Insect production systems and methods

ABSTRACT

Variable-scale, modular, easily manufacturable, energy efficient, reliable, and computer operated Insect Production Superstructure Systems (IPSS) may be used to produce insects for human and animal consumption, and for the extraction and use of lipids for applications involving medicine, nanotechnology, consumer products, and chemical production with minimal water, feedstock, and environmental impact. An IPSS may comprise modules including feedstock mixing, enhanced feedstock splitting, insect feeding, insect breeding, insect collection, insect grinding, pathogen removal, multifunctional flour mixing, liquid mixing, shaping, cooking, flavoring, biocatalyst mixing, exoskeleton separation, liquid separation, and lipid extraction. An IPSS may be configured to be constructed out of a plurality of containerized modules.

TECHNICAL FIELD

The present disclosure relates to the field of commercial scaleproduction of Orthoptera order of insects.

BACKGROUND

Efficient, reliable, and consistent computer operated insect rearingfacilities are needed to meet the insect production demands of society.In recent years, there has been an increasing demand for insect proteinfor human and animal consumption. There is also promise for theextraction and use of lipids from insects for applications involvingmedicine, nanotechnology, consumer products, and chemical production.Large scale insect production systems must be designed responsibly tomake sure that the insects are freed from hunger, thirst, discomfort,pain, injury, disease, fear and distress. These systems must beprecisely sized and situated to be able to provide systematically timedand controlled computer operated methods to maintain a sufficient amountof nutrition, to prevent disease, cannibalism, and injury. A need existsfor mass insect production facilities that maximize insect production ona small physical outlay while providing adequate space for high densityinsect rearing.

The ability to grow insects with minimal human interaction has been longregarded as desirable or needed to facilitate widespread use for humanand animal or consumption or for use as an intermediate lipid-basedproduct for the production of food and chemicals. In demographics, theworld population is the total number of humans currently living. As ofMarch 2016, it was estimated at 7.4 billion, an all-time record high.The United Nations estimates it will further increase to 11.2 billion inthe year 2100. World population has experienced continuous growth sincethe end of the Great Famine of 1315-17 and the Black Death in 1350, whenit was near 370 million.

In coming years, nuclear proliferation, food shortages, water scarcity,and diminishing petroleum reserves may result in a constraint on accessto food, water, chemicals, and other resources. Famine may resultcausing millions of deaths over an extended number of years which willmark a clear end to the period of growth and prosperity for the humancivilization, industrialization, and globalization.

The global population is expected to reach between 8.3 and 10.9 billionby 2050 which will be met with famine, malnutrition, and shortages ofclean drinking water. Further, the succession of major wars, famines,and other disasters may result in large-scale population losses if noalternate source or food and chemicals is immediately put in place.

Thus, it is of paramount importance that large-scale, modular, easilymanufacturable, energy efficient, reliable, computer operated insectproduction facilities are extensively deployed to produce insects forhuman and animal consumption, and for the extraction and use of lipidsfor applications involving medicine, nanotechnology, consumer products,and chemical production with minimal water, feedstock, and environmentalimpact.

There is a need for systems and methods that can clean and decontaminatewater from the most-harshest of environmental conditions and provide aclean water source suitable to feed and grow insects for human, animal,and chemical production. There is a need to develop and vastly implementlarge-scale, systematic insect feeding and breeding facilities that canaccommodate the protein and fatty acid demands of society. There is aneed to re-use old containerized shipping containers to promote theimplementation of widespread commercial production of insects to promoteregional, rural, and urban, job opportunities that maximizes the qualityof living the insects that are farmed.

There is a need for systems and methods that can produce unique andnovel foodstuffs or snack foods. There is a need for unique and novelfoodstuffs or snack foods to be created from Orthoptera order of insectsand produced from commercially available unit operations, including,feedstock mixing, enhanced feedstock splitting, insect feeding, insectbreeding, insect collection, insect grinding, pathogen removal,multifunctional flour mixing, liquid mixing, shaping, cooking,flavoring, biocatalyst mixing, exoskeleton separation, liquidseparation, and lipid extraction.

SUMMARY

This Summary is provided merely to introduce certain concepts and not toidentify any key or essential features of the claimed subject matter.

Paragraph A: A method for raising Orthoptera order of insects to producea flavored multifunctional flour mixture, the method comprising:

-   -   (a) providing a plurality of insect feeding chambers having        Orthoptera order of insects present therein;    -   (b) mixing feedstock with one or more from the group consisting        of water, mineral, vitamin, polymer, and an enhancer to form an        enhanced feedstock;    -   (c) apportioning the enhanced feedstock into a plurality of        enhanced feedstock streams;    -   (d) introducing the plurality of enhanced feedstock streams into        the plurality of insect feeding chambers to feed the insects        present therein;    -   (e) removing a portion of the insects from the plurality of        insect feeding chambers;    -   (f) grinding a portion of the removed insects to form ground        insects;    -   (g) mixing a portion of the ground insects with two or more from        the group consisting of cannabis enhancer, fiber-starch        material, binding agent, density improving textural supplement,        and moisture improving textural supplement to form a        multifunctional flour composition;    -   (h) mixing the multifunctional flour composition with water to        form a multifunctional flour and water mixture;    -   (i) pressurizing the multifunctional flour and water mixture to        form a pressurized multifunctional flour and water mixture;    -   (j) shaping the pressurized multifunctional flour and water        mixture to form a shaped multifunctional flour mixture;    -   (k) cooking the shaped multifunctional flour mixture to form a        cooked multifunctional flour mixture; and    -   (l) flavoring the cooked multifunctional flour mixture to form a        flavored multifunctional flour mixture;        wherein:

the Orthoptera order of insects are comprised of one or more from thegroup consisting of grasshoppers, crickets, cave crickets, Jerusalemcrickets, katydids, weta, lubber, acrida, and locusts;

the fiber-starch material is comprised of one or more from the groupconsisting of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, and vegetable-based materials;

the binding agent is comprised of one or more from the group consistingof agar, agave, alginin, arrowroot, carrageenan, collagen, cornstarch,egg whites, finely ground seeds, furcellaran, gelatin, guar gum, honey,katakuri starch, locust bean gum, pectin, potato starch, proteins,psyllium husks, sago, sugars, syrups, tapioca, vegetable gums, andxanthan gum;

the density improving textural supplement is comprised of one or morefrom the group consisting of extracted arrowroot starch, extracted cornstarch, extracted lentil starch, extracted potato starch, and extractedtapioca starch;

the moisture improving textural supplement is comprised of one or morefrom the group consisting of almonds, brazil nuts, cacao, cashews,chestnuts, coconut, filberts, hazelnuts, indian nuts, macadamia nuts,nut butters, nut oils, nut powders, peanuts, pecans, pili nuts, pinenuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tiger nuts, andwalnuts;

the mineral is comprised of one or more from the group consisting ofpotassium, chloride, sodium, calcium, phosphorous, magnesium, zinc,iron, manganese, copper, iodine, selenium, and molybdenum;

the vitamin is comprised of one or more from the group consisting ofvitamin B1, vitamin B2, vitamin E, and vitamin A;

the polymer is comprised of one or more from the group consisting of along-chain polymer of an N-acetylglucosamine, a derivative of glucose,chitin, cell walls of fungi, the exoskeleton of arthropods, theexoskeleton of arthropods crabs, the exoskeleton of arthropodscrustaceans, the exoskeleton of arthropods crabs, the exoskeleton ofarthropods lobsters, the exoskeleton of arthropods shrimp, theexoskeleton of arthropods insects, the radulae of mollusks, the beaks ofcephalopods, the shells of cephalopods, the beaks of squid, the beaks ofoctopuses, the scales of fish, the soft tissue of lissamphibians, andkeratin;

the enhancer is comprised of one or more from the group consisting ofniacin, taurine, glucuronic acid, malic acid, N-acetyl L tyrosine,L-phenylalanine, caffeine, citicoline, insect growth hormones, steroids,and human growth hormones;

the flavoring is comprised of one or more from the group consisting ofallspice berries, almond meal, anise seed, annato seed, arrowrootpowder, basil, bay leaves, black pepper, buttermilk, caraway, cayenne,celery seed, cheese cultures, chervil, Chile powder, chives, cilantro,cinnamon, citric acid, cloves, coconut shredded, coriander, corn oil,corn starch, cream of tartar, cubeb berries, cumin, curry, dextrose,dill, enzymes, fennel, fenugreek, file powder, garlic powder, ginger,grapefruit peel, green peppercorns, honey, horseradish powder, juniperberries, kaffir lime, lavender, lemon grass powder, lemon peel, limepeel, long pepper, marjoram, molasses, mustard, natural smoke flavor,nigella seeds, nutmeg, onion powder, orange peel, oregano, paprika,parsley, poppy seed, powdered cheese, red pepper, rose petals, rosemary,saffron, sage, salt, savory, sesame seed, star anise, sugar, sugarmaple, sumac, tamarind, tangerine peel, tarragon, thyme, tomatillopowder, tomato powder, torula yeast, turmeric, vanilla extract, wasabipowder, whey, white peppercorns, yeast extract, and yeast.

Paragraph B: The method according to Paragraph A, further comprising oneor more from the group consisting of:

-   -   (a) the fiber-starch material is mixed in step (g) ranging from        between 400 pounds of fiber-starch material per ton of        multifunctional flour composition to 1,800 pounds of        fiber-starch material per ton of multifunctional flour        composition;    -   (b) the binding agent is mixed in step (g) ranging from between        10 pounds of binding agent per ton of multifunctional flour        composition to 750 pounds of binding agent per ton of        multifunctional flour composition;    -   (c) the density improving textural supplement is mixed in        step (g) ranging from between 10 pounds of density improving        textural supplement per ton of multifunctional flour composition        to 1,000 pounds of density improving textural supplement per ton        of multifunctional flour composition;    -   (d) the moisture improving textural supplement is mixed in        step (g) ranging from between 10 pounds of moisture improving        textural supplements per ton of multifunctional flour        composition to 1,000 pounds of moisture improving textural        supplements per ton of multifunctional flour composition; and    -   (e) the cannabis enhancer is mixed in step (g) ranging from        between 25 pounds of cannabis enhancer per ton of        multifunctional flour composition to 1,800 pounds of cannabis        enhancer per ton of multifunctional flour composition.        Paragraph C: The method according to Paragraph A, further        comprising two or more from the group consisting of:

-   (a) mixing potassium at a potassium to enhanced feedstock ratio    ranging from between 0.5 pounds of potassium per ton of enhanced    feedstock to 250 pounds of potassium per ton of enhanced feedstock,

-   (b) mixing chloride at a chloride to enhanced feedstock ratio    ranging from between 0.5 pounds of chloride per ton of enhanced    feedstock to 250 pounds of chloride per ton of enhanced feedstock,

-   (c) mixing sodium at a sodium to enhanced feedstock ratio ranging    from between 0.5 pounds of sodium per ton of enhanced feedstock to    250 pounds of sodium per ton of enhanced feedstock,

-   (d) mixing calcium at a calcium to enhanced feedstock ratio ranging    from between 0.5 pound of calcium per ton of enhanced feedstock to    250 pounds of calcium per ton of enhanced feedstock,

-   (e) mixing phosphorous at a phosphorous to enhanced feedstock ratio    ranging from between 0.5 pounds of phosphorous per ton of enhanced    feedstock to 250 pounds of phosphorous per ton of enhanced    feedstock,

-   (f) mixing magnesium at a magnesium to enhanced feedstock ratio    ranging from between 0.5 pound of magnesium per ton of enhanced    feedstock to 150 pounds of magnesium per ton of enhanced feedstock,

-   (g) mixing zinc at a zinc to enhanced feedstock ratio ranging from    between 0.5 pounds of zinc per ton of enhanced feedstock to 150    pounds of zinc per ton of enhanced feedstock,

-   (h) mixing iron at an iron to enhanced feedstock ratio ranging from    between 0.5 pounds of iron per ton of enhanced feedstock to 150    pounds of iron per ton of enhanced feedstock,

-   (i) mixing manganese at a manganese to enhanced feedstock ratio    ranging from between 0.5 pounds of manganese per ton of enhanced    feedstock to 150 pounds of manganese per ton of enhanced feedstock,    and

-   (j) mixing copper at a copper to enhanced feedstock ratio ranging    from between 0.5 pounds of copper per ton of enhanced feedstock to    150 pounds of copper per ton of enhanced feedstock.    Paragraph D: A method according to Paragraph A, further comprising    freezing the insects after step (e) and before step (f).    Paragraph E: A method according to Paragraph A, further comprising    extracting lipids from a portion of the insects removed in step (e),    the method includes:    -   (a) providing a lipid extraction unit (1501) that is configured        to extract lipids from insects by use of a first immiscible        liquid (1506) and a second immiscible liquid (1507);    -   (b) introducing insects to the lipid extraction unit (1501);    -   (c) forming a first immiscible liquid and lipid mixture (1518)        comprised of a lipid portion and a first immiscible liquid        portion; and    -   (d) forming a second immiscible liquid and particulate mixture        (1521) comprised of a particulate portion and a second        immiscible liquid portion;        wherein the particulate portion is comprised of one or more from        the group consisting of insect legs, and wings, and protein.        Paragraph F: A method according to Paragraph A, further        comprising extracting lipids from a portion of the insects        removed in step (e), the method includes:    -   (a) providing a lipid extraction unit (1501) that includes a        mechanical lipid extraction unit (1501) that is configured to        pressurize insects to remove lipids therefrom;    -   (b) introducing insects to the mechanical lipid extraction unit        (1501);    -   (c) pressurizing the insects; and    -   (d) extracting liquid lipids from the insects.        Paragraph G: The method according to Paragraph A, wherein the        ground insects formed in step (f) are comprised of ground        Orthoptera order of insects having a bulk density ranging from        between 15 pounds per cubic foot to 50 pounds per cubic foot,        and include:    -   (a1) an energy content ranging from between 4,500 British        Thermal Units per pound to 10,500 British Thermal Units per        pound;    -   (a2) a hydrogen content ranging from between 2.5 weight percent        to 20 weight percent;    -   (a3) a carbon content ranging from between 15 weight percent to        55 weight percent;    -   (a4) an oxygen content ranging from between 15 weight percent to        55 weight percent;    -   (a5) a protein content ranging from between 45 weight percent to        85 weight percent;    -   (a6) a total fat content ranging from between 5 weight percent        to 60 weight percent;    -   (a7) potassium content ranging from between 25 ppm to 1 weight        percent;    -   (a8) calcium content ranging from between 50 ppm to 1 weight        percent;    -   (a9) three or more from the group consisting of:        -   (1) caffeine content ranging from between 50 ppm to 5 weight            percent,        -   (2) niacin content ranging from between 50 ppm to 5 weight            percent,        -   (3) taurine content ranging from between 50 ppm to 5 weight            percent,        -   (4) glucuronic acid content ranging from between 50 ppm to 5            weight percent,        -   (5) malic acid content ranging from between 50 ppm to 5            weight percent,        -   (6) N-acetyl L tyrosine content ranging from between 50 ppm            to 5 weight percent,        -   (7) L-phenylalanine content ranging from between 50 ppm to 5            weight percent,        -   (8) Vitamin B1 content ranging from between 15 ppm to 15            weight percent,        -   (9) Vitamin B2 content ranging from between 15 ppm to 15            weight percent,        -   (10) Vitamin B12 content ranging from between 15 ppm to 15            weight percent,        -   (11) Vitamin E content ranging from between 15 ppm to 15            weight percent,        -   (12) Vitamin A content ranging from between 15 ppm to 15            weight percent,        -   (13) oleic acid content ranging from between 5 weight            percent to 60 weight percent;        -   (14) linoleic acid content ranging from between 5 weight            percent to 60 weight percent,        -   (15) iron content ranging from between 25 ppm to 1500 ppm,        -   (16) sodium content ranging from between 1500 ppm to 5500            ppm,        -   (17) chloride content ranging from between 50 ppm to 1            weight percent,        -   (18) phosphorous content ranging from between 50 ppm to 1            weight percent,        -   (19) magnesium content ranging from between 50 ppm to 1            weight percent,        -   (20) zinc content ranging from between 50 ppm to 1 weight            percent,        -   (21) manganese content ranging from between 50 ppm to 1            weight percent,        -   (22) copper content ranging from between 50 ppm to 1 weight            percent,        -   (23) iodine content ranging from between 50 ppm to 1 weight            percent,        -   (24) selenium content ranging from between 50 ppm to 1            weight percent, and        -   (25) molybdenum content ranging from between 50 ppm to 1            weight percent;            wherein the Orthoptera order of insects are comprised of one            or more from the group consisting of grasshoppers, crickets,            cave crickets, Jerusalem crickets, katydids, weta, lubber,            acrida, and locusts.            Paragraph H: The method according to Paragraph A, further            comprising:

-   (a) providing:    -   (a1) a first water treatment unit (C10) including a cation        configured to remove positively charged ions from water to form        a positively charged ion depleted water (C29), the positively        charged ions are comprised of one or more from the group        consisting of calcium, magnesium, sodium, and iron;    -   (a2) a second water treatment unit (C11) including an anion        configured to remove negatively charged ions from the positively        charged ion depleted water (C29) to form a negatively charged        ion depleted water (C33), the negatively charged ions are        comprised of one or more from the group consisting of iodine,        chloride, and sulfate;    -   (a3) a third water treatment unit (C12) including a membrane        configured to remove undesirable compounds from the negatively        charged ion depleted water (C33) to form an undesirable        compounds depleted water (C36), the undesirable compounds are        comprised of one or more from the group consisting of dissolved        organic chemicals, viruses, bacteria, and particulates; and (a4)        a mixing tank (C15) configured to receive and mix the        undesirable compounds depleted water (C36) with multifunctional        flour to form a multifunctional flour and water mixture;

-   (b) providing a source of water;

-   (c) removing positively charged ions from the water of step (b) to    form a positively charged ion depleted water;

-   (d) removing negatively charged ions from the water after step (c)    to form a negatively charged ion depleted water;

-   (e) removing undesirable compounds from the water after step (d) to    form an undesirable compound depleted water; and

-   (f) mixing the undesirable compounds depleted water after step (e)    with the multifunctional flour to form a multifunctional flour and    water mixture.    Paragraph I: The method according to Paragraph A, further    comprising:

-   (a) providing:    -   (a1) a first water treatment unit (C10) including a cation        configured to remove positively charged ions from water to form        a positively charged ion depleted water (C29), the positively        charged ions are comprised of one or more from the group        consisting of calcium, magnesium, sodium, and iron;    -   (a2) a second water treatment unit (C11) including an anion        configured to remove negatively charged ions from the positively        charged ion depleted water (C29) to form a negatively charged        ion depleted water (C33), the negatively charged ions are        comprised of one or more from the group consisting of iodine,        chloride, and sulfate; and    -   (a3) a mixing tank (C15) configured to receive and mix the        negatively charged ion depleted water (C33) with multifunctional        flour to form a multifunctional flour and water mixture;

-   (b) providing a source of water;

-   (c) removing positively charged ions from the water of step (b) to    form a positively charged ion depleted water;

-   (d) removing negatively charged ions from the water after step (c)    to form a negatively charged ion depleted water;

-   (e) mixing a portion of the negatively charged ion depleted water    after step (d) with the multifunctional flour to form a    multifunctional flour and water mixture.    Paragraph J: The method according to Paragraph A, further    comprising:    -   (a) providing:        -   (a1) a refrigerant (Q31) that is configured to be            transferred from a compressor (Q30) to a condenser (Q32),            from the condenser (Q32) to an evaporator (Q34), and from            the evaporator (Q34) to the compressor (Q30);        -   (a2) the compressor (Q31) is in fluid communication with the            condenser (Q32);        -   (a3) the condenser (Q32) is in fluid communication with the            evaporator (Q34);        -   (a4) the evaporator (Q34) is in fluid communication with the            compressor (Q30), the evaporator (Q34) is configured to            evaporate the refrigerant (Q31) to absorb heat from the            interior (201) of the at least one feeding chamber (200,            FC1, FC2, FC3);    -   (b) removing heat from the interior of at least one feeding        chamber; and    -   (c) optionally condensing water vapor.        Paragraph K: The method according to Paragraph J, wherein:

-   the system is configured to operate in a plurality of modes of    operation, the modes of operation including at least:

-   a first mode of operation in which compression of a refrigerant    takes place within the compressor, and the refrigerant leaves the    compressor as a superheated vapor at a temperature above the    condensing point of the refrigerant;

-   a second mode of operation in which condensation of refrigerant    takes place within the condenser, heat is rejected and the    refrigerant condenses from a superheated vapor into a liquid, and    the liquid is cooled to a temperature below the boiling temperature    of the refrigerant; and

-   a third mode of operation in which evaporation of the refrigerant    takes place, and the liquid phase refrigerant boils in evaporator to    form a vapor or a superheated vapor while absorbing heat from the    interior of at least one feeding chamber.    Paragraph L: The method according to Paragraph A, further    comprising:

-   (a) providing an extrusion system (D12), the extrusion system (D12)    includes:    -   (a1) an auger (D14) driven by a motor (D16);    -   (a2) a die (D15) having a fixed cross-sectional profile and        configured to accept the multifunctional flour and water mixture        from the auger (D14) and produce a shaped multifunctional flour        mixture (D10);

-   (b) pressurizing the multifunctional flour and water mixture (C17)    with the auger (D14) to form a pressurized multifunctional flour and    water mixture (C17A); and

-   (c) passing the pressurized multifunctional flour and water mixture    (C17A) through the die (D15) to form a shaped multifunctional flour    mixture.    Paragraph M: The method according to Paragraph L, further    comprising:

-   (d) generating heat by forming the shaped multifunctional flour    mixture of step (c); and

-   (e) removing heat with a coolant.    Paragraph N: The method according to Paragraph A, further    comprising:

-   (a) providing a cooking module (14E) including an oven (E11) or a    fryer (E12), the cooking module (14E) is configured to accept and    cook the shaped multifunctional flour mixture (D10) to form a cooked    multifunctional flour mixture (E18A); and

-   (b) operating the oven (E11) or fryer (E12) at a temperature ranging    from between 100 degrees F. to 550 degrees F.;    wherein the fryer (E12) cooks the shaped multifunctional flour    mixture (D10) in an oil (E19), and the oil (E19) includes one or    more from the group consisting of lipids extracted from insects,    almond oil, animal-based oils, apricot kernel oil, avocado oil,    brazil nut oil, butter, canola oil, cashew oil, cocoa butter,    coconut oil, cooking oil, corn oil, cottonseed oil, fish oil,    grapeseed oil, hazelnut oil, hemp oil, insect oil, lard, lard oil,    macadamia nut oil, mustard oil, olive oil, palm kernel oil, palm    oil, peanut oil, rapeseed oil, rice oil, rice bran oil, safflower    oil, semi-refined sesame oil, semi-refined sunflower oil, sesame    oil, soybean oil, tallow of beef, tallow of mutton, vegetable oil,    and walnut oil.    Paragraph O: The method according to Paragraph A, further    comprising:

-   (a) providing a cooking module (14E) including a dryer (E13),    pressure cooker (E14), dehydrator (E15), or freeze dryer (E16), the    cooking module (14E) is configured to accept and cook the shaped    multifunctional flour mixture (D10) to form a cooked multifunctional    flour mixture (E18A); and

-   (b) cooking the shaped multifunctional flour mixture over a time    duration ranging from between 1 second to 60 minutes.    Paragraph P: The method according to Paragraph A, further    comprising:

-   (a) providing a flavoring machine (F12), the flavoring machine (F12)    is configured to provide contact between the flavoring (F18) and the    cooked multifunctional flour mixture (E18A) to form a flavored    multifunctional flour mixture (F10A); and

-   (b) flavoring the cooked multifunctional flour mixture (E18A) to    form a flavored multifunctional flour mixture (F10A).    Paragraph Q: The method according to Paragraph A, further    comprising:

-   (a) providing a flavoring machine (F12) including a tumbler (F13),    the tumbler (F13) has a motor (F14), the tumbler (F13) rotates and    is configured to provide contact between the flavoring (F18) and the    cooked multifunctional flour mixture (E18A) to form a flavored    multifunctional flour mixture (F10A); and

-   (b) flavoring the cooked multifunctional flour mixture (E18A) to    form a flavored multifunctional flour mixture (F10A);

wherein the tumbler (F13) rotates at a revolution per minute (RPM)ranging from between 3 RPM to 20 RPM.

Paragraph R: The method according to Paragraph A, further comprising:

-   (a) providing:    -   (a1) a first water treatment unit (G10) including a cation        configured to remove positively charged ions from water to form        a positively charged ion depleted water (G29), the positively        charged ions are comprised of one or more from the group        consisting of calcium, magnesium, sodium, and iron;    -   (a2) a second water treatment unit (G11) including an anion        configured to remove negatively charged ions from the positively        charged ion depleted water (G29) to form a negatively charged        ion depleted water (G33), the negatively charged ions are        comprised of one or more from the group consisting of iodine,        chloride, and sulfate;    -   (a3) a mixing tank (G15) configured to mix the negatively        charged ion depleted water (G33) with insects (G07, G08),        biocatalyst (G79), and also optionally with an acid (G79′) to        create an insect liquid biocatalyst mixture (G09), the mixing        tank (G15) is equipped with a heating jacket (G53J), the heating        jacket (G53J) has a heat transfer medium inlet (G90) and a heat        transfer medium outlet (G91), steam (G92) is introduced to the        heat transfer medium inlet (G90) to heat the insect liquid        biocatalyst mixture (G09);    -   (a4) a steam inlet conduit (G94) connected to the heat transfer        medium inlet (G90) and configured to transfer steam (G92) to the        heating jacket (G53J), and a steam supply valve (G95) interposed        on the steam inlet conduit (G94);    -   (a5) a transfer conduit (G50) connected at one end to the mixing        tank (G15) and at another end to a supply pump (G18), the supply        pump (G18) pressurizes the insect liquid biocatalyst mixture        (G09) to form a pressurized insect liquid biocatalyst mixture        (G09B);    -   (a6) an exoskeleton separator (H10) configured to remove        exoskeleton from the pressurized insect liquid biocatalyst        mixture (G09B) to form an exoskeleton-depleted insect liquid        mixture (H19) that has a reduced amount of exoskeleton (H46)        relative to the pressurized insect liquid biocatalyst mixture        (G09B);    -   (a7) a pump (H40) configured to pressurize the        exoskeleton-depleted insect liquid mixture (H39) to form a        pressurized exoskeleton-depleted insect liquid mixture (H41);    -   (a8) a liquid separator (I10) that is configured to remove        insects (I46) from the pressurized exoskeleton-depleted insect        liquid mixture (H41) to form an insect-depleted liquid mixture        (I19), the insect-depleted liquid mixture (I19) has a reduced        amount of insects (I46) relative to the pressurized        exoskeleton-depleted insect liquid mixture (H41);-   (b) providing a source of water;-   (c) removing positively charged ions from the water of step (b) to    form a positively charged ion depleted water;-   (d) removing negatively charged ions from the water after step (c)    to form a negatively charged ion depleted water;-   (e) introducing the negatively charged ion depleted water to the    mixing tank;-   (f) introducing a portion of the insects removed from the plurality    of insect feeding chambers into the mixing tank;-   (g) introducing a biocatalyst and optionally an acid to the mixing    tank to form an insect liquid biocatalyst mixture;-   (h) heating the insect liquid biocatalyst mixture of step (g);-   (i) pressurizing the insect liquid biocatalyst mixture after    step (h) to form a pressurized insect liquid biocatalyst mixture;-   (j) removing exoskeleton from the pressurized insect liquid    biocatalyst mixture to form an exoskeleton-depleted insect liquid    mixture that has a reduced amount of exoskeleton relative to the    pressurized insect liquid biocatalyst mixture;-   (k) pressurizing the exoskeleton-depleted insect liquid mixture to    form a pressurized exoskeleton-depleted insect liquid mixture;-   (l) removing insects from the pressurized exoskeleton-depleted    insect liquid mixture to form an insect-depleted liquid mixture, the    insect-depleted liquid mixture has a reduced amount of insects    relative to the pressurized exoskeleton-depleted insect liquid    mixture; and-   (m) mixing a portion of the insects removed in step (1) with one or    more from the group consisting of cannabis enhancer, fiber-starch    material, binding agent, density improving textural supplement, and    moisture improving textural supplement to form a multifunctional    flour composition;    wherein:

the biocatalyst is comprised of one or more from the group consisting ofan enzyme, casein protease, atreptogrisin A, flavorpro, peptidase,protease A, protease, aspergillus oryzae, bacillus subtilis, bacilluslicheniformis, aspergillus niger, aspergillus melleus, aspergilusoryzae, papain, carica papaya, bromelain, and ananas comorus stem;

the acid is comprised of one or more from the group consisting of anacid, abscic acid, acetic acid, ascorbic acid, benzoic acid, citricacid, formic acid, fumaric acid, hydrochloric acid, lactic acid, malicacid, nitric acid, organic acids, phosphoric acid, potassium hydroxide,propionic acid, salicylic acid, sulfamic acid, sulfuric acid, andtartaric acid;

the pressure drop across the steam supply valve (G95) ranges frombetween 5 pounds per square inch (PSI) to 200 PSI;

the exoskeleton separator (H10) is a filter;

the liquid separator (I10) is a filter, membrane, or an evaporator;

the fiber-starch material is comprised of one or more from the groupconsisting of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, and vegetable-based materials;

the binding agent is comprised of one or more from the group consistingof agar, agave, alginin, arrowroot, carrageenan, collagen, cornstarch,egg whites, finely ground seeds, furcellaran, gelatin, guar gum, honey,katakuri starch, locust bean gum, pectin, potato starch, proteins,psyllium husks, sago, sugars, syrups, tapioca, vegetable gums, andxanthan gum;

the density improving textural supplement is comprised of one or morefrom the group consisting of extracted arrowroot starch, extracted cornstarch, extracted lentil starch, extracted potato starch, and extractedtapioca starch;

the moisture improving textural supplement is comprised of one or morefrom the group consisting of almonds, brazil nuts, cacao, cashews,chestnuts, coconut, filberts, hazelnuts, indian nuts, macadamia nuts,nut butters, nut oils, nut powders, peanuts, pecans, pili nuts, pinenuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tiger nuts, andwalnuts.

Paragraph S: A method to produce a multifunctional flour composition,the method includes:

-   (a) providing:    -   (a1) a first water treatment unit (G10) including a cation        configured to remove positively charged ions from water to form        a positively charged ion depleted water (G29), the positively        charged ions are comprised of one or more from the group        consisting of calcium, magnesium, sodium, and iron;    -   (a2) a second water treatment unit (G11) including an anion        configured to remove negatively charged ions from the positively        charged ion depleted water (G29) to form a negatively charged        ion depleted water (G33), the negatively charged ions are        comprised of one or more from the group consisting of iodine,        chloride, and sulfate;    -   (a3) a mixing tank (G15) configured to mix the negatively        charged ion depleted water (G33) with whole insects (G07) or        ground insects (G08) and a biocatalyst to create an insect        liquid biocatalyst mixture (G09), the mixing tank (G15) is        equipped with a heating jacket (G53J), the heating jacket (G53J)        has a heat transfer medium inlet (G90) and a heat transfer        medium outlet (G91), steam (G92) is introduced to the heat        transfer medium inlet (G90) to heat the insect liquid        biocatalyst mixture (G09);    -   (a4) a steam inlet conduit (G94) connected to the heat transfer        medium inlet (G90) and configured to transfer steam (G92) to the        heating jacket (G53J), and a steam supply valve (G95) interposed        on the steam inlet conduit (G94);    -   (a5) a transfer conduit (G50) connected at one end to the mixing        tank (G15) and at another end to a supply pump (G18), the supply        pump (G18) pressurizes the insect liquid biocatalyst mixture        (G09) to form a pressurized insect liquid biocatalyst mixture        (G09B);    -   (a6) an exoskeleton separator (H10) configured to remove        exoskeleton from the pressurized insect liquid biocatalyst        mixture (G09B) to form an exoskeleton-depleted insect liquid        mixture (H19) that has a reduced amount of exoskeleton (H46)        relative to the pressurized insect liquid biocatalyst mixture        (G09B);    -   (a7) a pump (H40) configured to pressurize the        exoskeleton-depleted insect liquid mixture (H39) to form a        pressurized exoskeleton-depleted insect liquid mixture (H41);    -   (a8) a liquid separator (I10) that is configured to remove        insects (I46) from the pressurized exoskeleton-depleted insect        liquid mixture (H41) to form an insect-depleted liquid mixture        (I19), the insect-depleted liquid mixture (I19) has a reduced        amount of insects (I46) relative to the pressurized        exoskeleton-depleted insect liquid mixture (H41);-   (b) providing a source of water;-   (c) removing positively charged ions from the water of step (b) to    form a positively charged ion depleted water;-   (d) removing negatively charged ions from the water after step (c)    to form a negatively charged ion depleted water;-   (e) introducing the negatively charged ion depleted water to the    mixing tank;-   (f) introducing whole insects or ground insects and biocatalyst to    the mixing tank to form an insect liquid biocatalyst mixture;-   (g) heating the insect liquid biocatalyst mixture of step (f);-   (h) pressurizing the insect liquid biocatalyst mixture after    step (g) to form a pressurized insect liquid biocatalyst mixture;-   (i) removing exoskeleton from the pressurized insect liquid    biocatalyst mixture to form an exoskeleton-depleted insect liquid    mixture that has a reduced amount of exoskeleton relative to the    pressurized insect liquid biocatalyst mixture;-   (j) pressurizing the exoskeleton-depleted insect liquid mixture to    form a pressurized exoskeleton-depleted insect liquid mixture;-   (k) removing insects from the pressurized exoskeleton-depleted    insect liquid mixture to form an insect-depleted liquid mixture, the    insect-depleted liquid mixture has a reduced amount of insects    relative to the pressurized exoskeleton-depleted insect liquid    mixture; and-   (l) mixing a portion of the insects removed in step (k) with one or    more from the group consisting of cannabis enhancer, fiber-starch    material, binding agent, density improving textural supplement, and    moisture improving textural supplement to form a multifunctional    flour composition;    wherein:

the biocatalyst is comprised of one or more from the group consisting ofan enzyme, casein protease, atreptogrisin A, flavorpro, peptidase,protease A, protease, aspergillus oryzae, bacillus subtilis, bacilluslicheniformis, aspergillus niger, aspergillus melleus, aspergilusoryzae, papain, carica papaya, bromelain, and ananas comorus stem;

the pressure drop across the steam supply valve (G95) ranges frombetween 5 pounds per square inch (PSI) to 200 PSI;

the fiber-starch material is comprised of one or more from the groupconsisting of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, and vegetable-based materials;

the binding agent is comprised of one or more from the group consistingof agar, agave, alginin, arrowroot, carrageenan, collagen, cornstarch,egg whites, finely ground seeds, furcellaran, gelatin, guar gum, honey,katakuri starch, locust bean gum, pectin, potato starch, proteins,psyllium husks, sago, sugars, syrups, tapioca, vegetable gums, andxanthan gum;

the density improving textural supplement is comprised of one or morefrom the group consisting of extracted arrowroot starch, extracted cornstarch, extracted lentil starch, extracted potato starch, and extractedtapioca starch;

the moisture improving textural supplement is comprised of one or morefrom the group consisting of almonds, brazil nuts, cacao, cashews,chestnuts, coconut, filberts, hazelnuts, indian nuts, macadamia nuts,nut butters, nut oils, nut powders, peanuts, pecans, pili nuts, pinenuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tiger nuts, andwalnuts.

Paragraph T: A method to produce a multifunctional flour composition,the method includes:

-   (a) providing:    -   (a1) a first water treatment unit (G10) including a cation        configured to remove positively charged ions from water to form        a positively charged ion depleted water (G29), the positively        charged ions are comprised of one or more from the group        consisting of calcium, magnesium, sodium, and iron;    -   (a2) a second water treatment unit (G11) including an anion        configured to remove negatively charged ions from the positively        charged ion depleted water (G29) to form a negatively charged        ion depleted water (G33), the negatively charged ions are        comprised of one or more from the group consisting of iodine,        chloride, and sulfate;    -   (a3) a mixing tank (G15) configured to mix the negatively        charged ion depleted water (G33) with insects and a biocatalyst        to create an insect liquid biocatalyst mixture (G09), the mixing        tank (G15) is equipped with a heat exchanger (G53) that is        configured to heat the insect liquid biocatalyst mixture (G09);    -   (a4) a transfer conduit (G50) connected at one end to the mixing        tank (G15) and at another end to a supply pump (G18), the supply        pump (G18) pressurizes the insect liquid biocatalyst mixture        (G09) to form a pressurized insect liquid biocatalyst mixture        (G09B);    -   (a5) an exoskeleton separator (H10) configured to remove        exoskeleton from the pressurized insect liquid biocatalyst        mixture (G09B) to form an exoskeleton-depleted insect liquid        mixture (H19) that has a reduced amount of exoskeleton (H46)        relative to the pressurized insect liquid biocatalyst mixture        (G09B);    -   (a6) a pump (H40) configured to pressurize the        exoskeleton-depleted insect liquid mixture (H39) to form a        pressurized exoskeleton-depleted insect liquid mixture (H41);    -   (a7) a liquid separator (I10) that is configured to remove        insects (I46) from the pressurized exoskeleton-depleted insect        liquid mixture (H41) to form an insect-depleted liquid mixture        (I19), the insect-depleted liquid mixture (I19) has a reduced        amount of insects (I46) relative to the pressurized        exoskeleton-depleted insect liquid mixture (H41);-   (b) providing a source of water;-   (c) removing positively charged ions from the water of step (b) to    form a positively charged ion depleted water;-   (d) removing negatively charged ions from the water after step (c)    to form a negatively charged ion depleted water;-   (e) introducing the negatively charged ion depleted water to the    mixing tank;-   (f) introducing insects and biocatalyst to the mixing tank to form    an insect liquid biocatalyst mixture;-   (g) heating the insect liquid biocatalyst mixture of step (f);-   (h) pressurizing the insect liquid biocatalyst mixture after    step (g) to form a pressurized insect liquid biocatalyst mixture;-   (i) removing exoskeleton from the pressurized insect liquid    biocatalyst mixture to form an exoskeleton-depleted insect liquid    mixture that has a reduced amount of exoskeleton relative to the    pressurized insect liquid biocatalyst mixture;-   (j) pressurizing the exoskeleton-depleted insect liquid mixture to    form a pressurized exoskeleton-depleted insect liquid mixture;-   (k) removing insects from the pressurized exoskeleton-depleted    insect liquid mixture to form an insect-depleted liquid mixture, the    insect-depleted liquid mixture has a reduced amount of insects    relative to the pressurized exoskeleton-depleted insect liquid    mixture; and-   (l) mixing a portion of the insects removed in step (k) with one or    more from the group consisting of cannabis enhancers, fiber-starch    materials, binding agents, density improving textural supplements,    and moisture improving textural supplements to form a    multifunctional flour composition;

wherein:

the biocatalyst is comprised of one or more from the group consisting ofan enzyme, casein protease, atreptogrisin A, flavorpro, peptidase,protease A, protease, aspergillus oryzae, bacillus subtilis, bacilluslicheniformis, aspergillus niger, aspergillus melleus, aspergilusoryzae, papain, carica papaya, bromelain, and ananas comorus stem;

the fiber-starch materials are comprised of one or more from the groupconsisting of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, and vegetable-based materials;

the binding agents are comprised of one or more from the groupconsisting of agar, agave, alginin, arrowroot, carrageenan, collagen,cornstarch, egg whites, finely ground seeds, furcellaran, gelatin, guargum, honey, katakuri starch, locust bean gum, pectin, potato starch,proteins, psyllium husks, sago, sugars, syrups, tapioca, vegetable gums,and xanthan gum;

the density improving textural supplements are comprised of one or morefrom the group consisting of extracted arrowroot starch, extracted cornstarch, extracted lentil starch, extracted potato starch, and extractedtapioca starch;

the moisture improving textural supplements are comprised of one or morefrom the group consisting of almonds, brazil nuts, cacao, cashews,chestnuts, coconut, filberts, hazelnuts, indian nuts, macadamia nuts,nut butters, nut oils, nut powders, peanuts, pecans, pili nuts, pinenuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tiger nuts, andwalnuts.

DESCRIPTION OF THE DRAWINGS

Reference will now be made in detail to various embodiments of thedisclosure. Each embodiment is provided by way of explanation of thedisclosure, not limitation of the disclosure. In fact, it will beapparent to those skilled in the art that modifications and variationscan be made in the disclosure without departing from the teaching andscope thereof. For instance, features illustrated or described as partof one embodiment to yield a still further embodiment derived from theteaching of the disclosure. Thus, it is intended that the disclosure orcontent of the claims cover such derivative modifications and variationsto come within the scope of the disclosure or claimed embodimentsdescribed herein and their equivalents.

Additional objects and advantages of the disclosure will be set forth inpart in the description which follows, and in part will be obvious fromthe description, or may be learned by practice of the claims. Theobjects and advantages of the disclosure will be attained by means ofthe instrumentalities and combinations and variations particularlypointed out in the appended claims.

The accompanying figures show schematic process flowcharts of preferredembodiments and variations thereof. A full and enabling disclosure ofthe content of the accompanying claims, including the best mode thereofto one of ordinary skill in the art, is set forth more particularly inthe remainder of the specification, including reference to theaccompanying figures showing how the preferred embodiments and othernon-limiting variations of other embodiments described herein may becarried out in practice, in which:

FIG. 1A shows a simplistic block flow diagram of one embodiment of anInsect Production Superstructure System (IPSS) including the sequencesteps of feedstock mixing (step A), feedstock splitting (step B), insectfeeding (step C1, C2), insect breeding (step D), insect collection (stepE), and insect grinding (step F).

FIG. 1B elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence steps of pathogen removal (step G) andmultifunctional flour mixing (step H).

FIG. 1C elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence step of lipid extraction (step J).

FIG. 2 shows a non-limiting embodiment of an enhanced feedstock mixingmodule (1000) including a feedstock distribution module (1A), mineraldistribution module (1B), vitamin distribution module (1C), polymerdistribution module (1D), water distribution module (1E), and anenhanced feedstock distribution module (1F).

FIG. 3 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein the egg transfer system (244) of theinsect feeding module (2000) is at a first state in a first retractedheight (H1).

FIG. 4 shows one non-limiting embodiment of a network (220) of cells(219) for growing insects within a feeding chamber (200) of the insectfeeding module (2000) shown in FIG. 3.

FIG. 5 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a second mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a second state at a second elevated height (H2) so as topermit insects (225) to lay eggs (259) within a provided breedingmaterial (248).

FIG. 6 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a third mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a first state in a first retracted height (H1) so as todiscontinue insects (225) from laying eggs (259) within the providedbreeding material (248).

FIG. 7 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) and insect evacuation module (3000)operating in a fourth mode of operation wherein a vibration unit (214)is activated to permit the removal of insects (225) from the network(220) of cells (219) and wherein the insect evacuation module (3000)separates insects from gas while a vacuum is pulled on the insectfeeding module (2000) via an insect evacuation fan (312)

FIG. 8 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein a plurality of slats (341) of an eggtransfer system (244) of the insect feeding module (2000) are in firstclosed state (341A).

FIG. 9 elaborates upon the non-limiting embodiment of FIG. 8 and showsbreeding material (248) resting upon the surface of the plurality ofslats (341) of the egg transfer system (244) so as to permit insects(225) to lay eggs (259) within the breeding material (248).

FIG. 10 elaborates upon the non-limiting embodiment FIG. 8 but shows theegg transfer system (244) in a second open state (341A) so as to permitegg-laden breeding material (248) to pass through the plurality of slats(341) while the vibration unit (214) is activated, some insects (225)may pass through the open slats (341) as well.

FIG. 11 shows a simplistic diagram illustrating an insect grindingmodule that is configured to grind at least a portion of the insectstransferred from the insect evacuation module (3000).

FIG. 12A shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000) by useof at least one solvent.

FIG. 12B shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000) byusing of no solvent by way of an expeller press.

FIG. 13 shows a simplistic diagram illustrating a pathogen removalmodule that is configured to remove pathogens from at least a portion ofthe insects transferred from the insect evacuation module (3000).

FIG. 14A shows a simplistic diagram illustrating a multifunctional flourmixing module that is configured to generate a multifunctional flourfrom at least a portion of the insects transferred from the pathogenremoval module and including the sequence steps or sub-modules includingan insect distribution module (6A), fiber-starch distribution module(6B), binding agent distribution module (6C), density improving texturalsupplement distribution module (6D), moisture improving texturalsupplement distribution module (6E), multifunctional flour mixing module(6F).

FIG. 14B shows a simplistic diagram illustrating a multifunctional flourmixing module that is configured to generate a multifunctional flour asdescribed in FIG. 14A however instead from at least a portion of theinsects transferred from the insect grinding module.

FIG. 14C shows one non-limiting embodiment of a liquid mixing module(LMM) that is configured to mix water with multifunctional flour (6F23)provided from the multifunctional flour mixing module as shown in FIG.14A or 14B.

FIG. 14D shows one non-limiting embodiment of a shaping module (14D)that is configured to shape the multifunctional flour and water mixture(C17) to produce a shaped multifunctional flour mixture (D10).

FIG. 14E shows one non-limiting embodiment of a cooking module (14E)that is configured to cook the shaped multifunctional flour mixture(D10) provided from the shaping module (14D) to form a cookedmultifunctional flour mixture (E18A).

FIG. 14F shows one non-limiting embodiment of a flavoring module (14F)that is configured to flavor the cooked multifunctional flour mixture(E18A) provided from the cooking module (14E) to form a flavoredmultifunctional flour mixture (F10).

FIG. 14G shows one non-limiting embodiment of a biocatalyst mixingmodule (14G) that is configured to mix insects, water, biocatalyst, andoptionally acid to create an insect liquid biocatalyst mixture (G09).

FIG. 14H shows one non-limiting embodiment of an exoskeleton separationmodule (14H) that is configured to remove the exoskeleton containedwithin the insect liquid biocatalyst mixture (G09).

FIG. 14I shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from the exoskeleton-depletedinsect liquid mixture (H39) to provide an insect-depleted liquid mixture(I19) and insects (I46).

FIG. 14J shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from the exoskeleton-depletedinsect liquid mixture (H39) to produce a vaporized liquid (J22) and astream of liquid-depleted insects (J10).

FIG. 15 shows a simplistic diagram illustrating a plurality of feedingchambers (FC1, FC2, FC3) of an insect feeding module (2000) integratedwithin one common separator (300) of an insect evacuation module (3000).

FIG. 16 shows a simplistic diagram illustrating a plurality ofseparators (S1, S2, S3) integrated with one common feeding chamber(FC1), and wherein the feeding chamber (FC1) and second separator (S2)are in fluid communication with one common breeding chamber (BC), andwherein the breeding chamber (BC) is in fluid communication with onecommon breeding material and insect separator (SEPIA), and wherein thebreeding material and insect separator (SEPIA) is in fluid communicationwith at least one of a plurality of feeding chambers (FC1, FC2, FC3).

FIG. 17 shows a perspective view of one embodiment of a scalableportable modular Insect Production Superstructure System (IPSS) designedwith: one enhanced feedstock mixing module (1000); three insect feedingmodules (2000A, 2000B, 2000C); one insect evacuation module (3000);three insect breeding modules (4000A, 4000B, 4000C), and three insectseparation modules (5000).

FIG. 18 shows a front view of one embodiment of an enhanced feedstockmixing module (1000) module including a feedstock distribution module(1A), mineral distribution module (1B), vitamin distribution module(1C), and a polymer distribution module (1D).

FIG. 19 shows a top view of one embodiment of an enhanced feedstockmixing module (1000) including a feedstock distribution module (1A),mineral distribution module (1B), vitamin distribution module (1C), anda polymer distribution module (1D).

FIG. 20 shows a first side view of one embodiment of an enhancedfeedstock mixing module (1000).

FIG. 21 shows a front view of one embodiment of a water distributionmodule (1E).

FIG. 22 shows a top view of one embodiment of a water distributionmodule (1E).

FIG. 23 shows a first side view of one embodiment of a waterdistribution module (1E).

FIG. 24 shows a front view of one embodiment of an enhanced feedstockdistribution module (1F).

FIG. 25 shows a top view of one embodiment of an enhanced feedstockdistribution module (1F).

FIG. 26 shows a first side view of one embodiment of an enhancedfeedstock distribution module (1F).

FIG. 27A shows a front view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C).

FIG. 28A shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C).

FIG. 27B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one cube container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 27C shows a top view of one embodiment of an insect feeding module(2000, 24000A, 2000B, 2000C) equipped with a humidity control unit(HCU).

FIG. 28B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one cube container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 29 shows a first side view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C).

FIG. 30 shows a front view of one embodiment of an insect evacuationmodule (3000).

FIG. 31 shows a top view of one embodiment of an insect evacuationmodule (3000).

FIG. 32 shows a first side view of one embodiment of an insectevacuation module (3000).

FIG. 33 shows a front view of one embodiment of an insect breedingmodule (4000, 4000A).

FIG. 34 shows a top view of one embodiment of an insect breeding module(4000, 4000A).

FIG. 34A shows a top view of one embodiment of an insect breeding module(4000, 4000A, 4000B, 4000C) equipped with a humidity control unit (HCU).

FIG. 35 shows a first side view of one embodiment of an insect breedingmodule (4000, 4000A) at a cutaway section of the conveyor side view(CSV).

FIG. 36 shows a second side view of one embodiment of an insect breedingmodule (4000, 4000A) at a cutaway section of the conveyor side view(CSV).

FIG. 37 shows a front view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 38 shows a top view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 39 shows a first side view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 40A shows Table 1 with upper and lower ranges of feedstock mineralenhancers, feedstock vitamin enhancers, feedstock polymer enhancers, andother ‘Energy-Insect™’ enhancers.

FIG. 40B shows one non-limiting example of process conditions within anInsect Production Superstructure System (IPSS).

FIG. 40C shows nutritional requirements of insects produced in an InsectProduction Superstructure System (IPSS) that are fed an enhancedfeedstock.

FIG. 41A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 41B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 42A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 42B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 43A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 43B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 44A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 44B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 45A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects to generate a multifunctional flourcomposition.

FIG. 45B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional flourcomposition.

FIG. 46 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional flourcomposition.

FIG. 47 shows one non-limiting embodiment of a method for raisingOrthoptera order of insects for the separation of lipids containedwithin said insects.

FIG. 48 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects for the extraction of lipids

FIG. 1A

FIG. 1A shows a simplistic block flow diagram of one embodiment of anInsect Production Superstructure System (IPSS) including the sequencesteps of feedstock mixing (step A), feedstock splitting (step B), insectfeeding (step C1, C2), insect breeding (step D), insect collection (stepE), and insect grinding (step F).

FIG. 1A shows a plurality of sequence steps of an Insect ProductionSuperstructure System (IPSS) including, feedstock mixing (step A),feedstock splitting (step B), insect feeding chamber #1 (step C1),insect feeding chamber #2 (step C2), insect breeding (step D), insectcollection (step E), and insect grinding (step F).

Step A involves feedstock mixing where feedstock may be mixed with oneor more additives from the group consisting of water, minerals,vitamins, and polymer to form an enhanced feedstock. Additionally, otherenhancers may be added to the feedstock such as niacin, taurine,glucuronic acid, malic acid, N-acetyl L tyrosine, L-phenylalanine,caffeine, citicoline, or insect growth hormones. Table 1 on FIG. 40lists the types of additives and enhancers that may be mixed with afeedstock to generate an enhanced feedstock.

Generally, a feedstock may be characterized as agriculture residue,alcohol production coproducts, animal waste, bio-waste, compost, cropresidues, energy crops, fermentation waste, meat, insects, fermentativeprocess wastes, food processing residues, food waste, garbage,industrial waste, livestock waste, municipal solid waste, plant matter,poultry wastes, rice straw, sewage, spent grain, spent microorganisms,urban waste, vegetative material, or wood waste.

Mixing of feedstock with additives or enhancers is discussed below indetail. Exact proportions of feedstock, additives, and enhancers may beprecisely combined to form an enhanced feedstock that is suitable togrow insects in a manner that maximizes productivity, minimizesmortality, and maximizes animal welfare. It has been my realization thatthe enhanced feedstock mixtures, weigh ratios, proportions, ranges citedin Table 1 of FIG. 40 are those that maximize insect production in aminimal amount of space.

It also has been my realization that the enhancers listed herein arethose, when fed to insects, may then subsequently fed to humans asEnergy-Insects™, which are a specialized kind of edible insect thatcontains a dose of the stimulant caffeine, vitamins, and otherfunctional ingredients. It has also been my realization that insectstruly enjoy eating my inventive enhanced feedstock blend and itincreases their quality of life. Although there is no evidence and noway of truly telling that insects have the cognitive ability to enjoyeating my proprietary enhanced feedstock blend, I certainly give themthe benefit of the doubt.

It has also been my realization that mixing water with the feedstockprofoundly benefits insects since it elevates their well-being by makingit impossible for them not to fear from expiration from respiratoryimpairment from being drowned in or under a liquid. It is the totalityof the features of the present application that provide the maximumbenefit to society.

An enhanced feedstock transfer line (002) is discharged from feedstockmixing (step A) where it enters the feedstock splitting (step B). Step Bfeedstock splitting involves dividing the enhanced feedstock up into aplurality of enhanced feedstock steams. In embodiments, it may beadvantageous to have a plurality of insect feeding chambers and only onefeedstock mixing sequence step. This minimizes the capital intensity ofthe Insect Production Superstructure System (IPSS) to thus in turnpermits a more lucrative return on investment (ROI). In some instances,Step B may not be required since only one feeding chamber is desired.

A first enhanced feedstock transfer line (004) and a second enhancedfeedstock transfer line (006) are discharged from feedstock splitting(Step B) and are routed to insect feeding chamber #1 (step C1) andinsect feeding chamber #2 (step C2). FIG. 1A discloses a plurality offeeding chamber steps (C1 and C2). Two feeding chambers are shown inFIG. 1A, however it is to be noted that only one may be utilized, orthree (as depicted in FIG. 17), or more may be utilized as seen fit.

Although two feeding chambers are shown in FIG. 1A, it is to be notedthat the egg-laying insects present therein may freely travel from onefeeding chamber to another. This is evidenced by feeding chambertransfer line (008) which connects the insect feeding chamber #1 (stepC1) with insect feeding chamber #2 (step C2). The plurality of feedingchambers and a passageways therebetween encourage egg-laying insectstherein to express normal behavior by enabling mobility and relocationto a more suitable living environment. An insect may decide to up andrelocate for any reason it chooses or no reason at all. In the eventthat one breeding chamber lacks sufficient amounts of enhancedfeedstock, or is over-crowded, or contains diseased or cannibalisticinsects, the insects may relocate to another feeding chamber toalleviate their discomfort, pain, injury, disease, and fear anddistress.

Herein is disclosed an Insect Production Superstructure System (IPSS)that permits insects to have mobility and the opportunity to choosebetween different possible courses of action. Herein are disclosedadvancements and better solutions that meet new requirements,unarticulated needs, or existing market needs in maximizing insectwelfare, maximizing insect output on a minimal physical outlay, andbenefit of large groups of people a high-value animal protein.

FIG. 1A shows a first egg-laden breeding material transfer line (020)and a second egg-laden breeding material transfer line (021) being mixedinto a combined egg-laden breeding material transfer line (022) which isthen in turn provided to insect breeding (step D).

Insect eggs are extracted from the plurality of breeding chambers andare provided to a breeding chamber where the eggs are incubated andhatched. Hatched insects are then provided to the plurality of insectfeeding chambers (step C1 and C2) via a first feeding chamber hatchedinsect transfer line (024) and a second feeding chamber hatched insecttransfer line (026), respectively. Thus herein is disclosed a method to:(i) remove at least a portion of eggs laid by the egg-laying insectswithin the feeding chambers; (ii) incubate at least a portion of theremoved eggs in a breeding chamber; (iii) hatch at least a portion ofincubated eggs; and, (iv) introduce a portion of hatched insects backinto the insect feeding chamber.

Generally, the innovative methods of the Insect ProductionSuperstructure System (IPSS) is more generally suited for insects of theOrthoptera order of insects including grasshoppers, crickets, cavecrickets, Jerusalem crickets, katydids, weta, lubber, acrida, andlocusts. However, other methods and systems described herein may also beapplied towards other orders of insects, such as cicadas, or evenminilivestock if desired.

Both the insect feeding chamber #1 (step C1) and insect feeding chamber#2 (step C2) are in fluid communication with insect collection (step E).The insect feeding chamber #1 (step C1) is in fluid communication withinsect collection (step E) via a first feeding chamber insect transferline (010). The insect feeding chamber #2 (step C2) is in fluidcommunication with insect collection (step E) via a second feedingchamber insect transfer line (012).

Insects may be collected from the insect feeding chambers in a number ofways. Some non-limiting embodiments of the present disclosure suggestremoving the insects by vibrating the egg-laying insects from thefeeding chamber. Some non-limiting embodiments of the present disclosuresuggest removing the insects by conveying the egg-laying insects fromthe feeding chamber. Some non-limiting embodiments of the presentdisclosure suggest vacuuming the insects from the feeding chamber.

It is to be noted that all of the embodiments disclosed herein arenon-limiting and as long as the insects are in fact removed from aninsect feeding chamber by any conceivable means or method, the bounds ofthis application are deemed to have been infringed. Thus, it should beapparent, however, to those skilled in the art that many moremodifications besides those already described are possible withoutdeparting from the inventive concepts herein related to removing insectsfrom the feeding chamber. The inventive subject matter pertaining toremoving insects from the feeding chambers, therefore, is not to berestricted to vibrating, conveying, vacuuming insects from the feedingchamber but instead extend to any possible means for achieving the endof removing insects from out of the interior of the feeding chamber.

In embodiments, the insect collection (step E) is in fluid communicationwith insect grinding (step F) via a combined collected insect transferline (014). The insect grinding (step F) is configured to output groundinsects via a ground insect transfer line (016).

FIG. 1B

FIG. 1B elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence steps of pathogen removal (step G) andmultifunctional flour mixing (step H).

FIG. 1B shows a pathogen removal (step G) placed upstream of amultifunctional flour mixing (step H) step. In embodiments, the pathogenremoval (step G) is configured to accept collected insects provided fromthe insect collection (step E) or insect grinding (step F). Inembodiments, the pathogen removal (step G) is configured to acceptcollected insects provided from the insect collection (step E). Inembodiments, the pathogen removal (step G) is configured to acceptcollected insects provided from the insect grinding (step F) as seen inFIG. 13 as accepting ground separated insects (1500). However, it is tobe noted that grinding need not take place in order for pathogen to beremoved from collected insects. As seen in the non-limiting embodimentof FIG. 1B, pathogen removal (step G) only places after insectcollection (step E) and after insect grinding (step F). However, it isnot necessary that grinding takes place in between insect collection(step E) and pathogen removal (step G).

Pathogen removal (step G) is optional. Until we know for sure that adeath by being grinded up is not less painful than being microwaved, wewill give the insects the benefit of the doubt and concede to the notionthat sudden, instantaneous death will lead to less stress and sufferingas opposed to being microwaved over up to about 500 seconds. Thus, it isthe essence of this disclosure to intend that a person of ordinary skillin the art be on notice of my intention to entertain all possibilitiesto grinding insects, microwaving them, or suffocating them to death.Until there is peer-reviewed evidence to suggest that grinding is leastdeleterious on the welfare of an insect, Step F will be before Step G.

In embodiments, insects may be euthanized by hypothermia. Inembodiments, insects may be euthanized by freezing them. In embodiments,insects may be euthanized by reducing the temperature to below 32degrees Fahrenheit. In embodiments, insects may be euthanized byreducing the temperature to below 40 degrees Fahrenheit.

Pathogen Removal (Step G)

The pathogen removal (step G) involves utilization of a pathogen removalunit to convert a stream of pathogen-laden insects into a stream ofpathogen-depleted insects (1570). The pathogen removal (step G) removespathogens from pathogen-laden insects to form pathogen depleted insectswhich has a reduced amount of pathogens relative to the pathogen-ladeninsects.

In embodiments, pathogens are comprised of one or more from the groupconsisting of acute respiratory syndrome coronavirus, influenza Aviruses, H5N1, H7N7, avian influenza, foot and mouth disease, bovinespongiform encephalopathy, Q-fever, cutaneous zoonotic leishmaniasis,Ebola, monkeypox, Rift Valley fever, Crimea Congo hemorrhagic fever,encephalopathy, West Nile fever, paramyxoviruses, viruses, bacteria,fungus, prions, and parasites. In embodiments, some of the aforesaidpathogens may be present in the insects that grow within the feedingchamber. It is possible that the water added to the enhanced feedstockcontains pathogens as listed above which the insect's carry-on throughto the humans and animals during consumption. Thus, it is of paramountimportance to mitigate the possible threats to society that areassociated with permitting pathogen-laden water to pass on to humans oranimals via the pathogen-laden insects.

In embodiments, pathogens are removed from the insects by theapplication of heat. In embodiments, pathogens are removed by heatinginsects to a temperature range between about 110 degrees Fahrenheit toabout 550 degrees Fahrenheit. In embodiments, pathogens are removed byheating insects to a temperature range between about 120 degreesFahrenheit to about 170 degrees Fahrenheit. In embodiments, pathogensare removed by heating said insects to a temperature range between about171 degrees Fahrenheit to about 250 degrees Fahrenheit. In embodiments,pathogens are removed by heating insects to a temperature range betweenabout 350 degrees Fahrenheit to about 450 degrees Fahrenheit.

In embodiments, pathogens are removed from said insects with microwaveradiation. In embodiments, the microwave radiation is in the form ofvariable frequency microwave radiation. In embodiments, the variablefrequency microwave radiation operates at a frequency between about 2GHz to about 8 GHz. In embodiments, the variable frequency microwaveradiation operates at a frequency of about 2.45 GHz.

In embodiments, the variable frequency microwave radiation operates at apower level between about 30 Watts to about 500 Watts. In embodiments,the variable frequency microwave radiation operates at a power levelbetween about 50 Watts to about 150 Watts. In embodiments, the variablefrequency microwave radiation operates at a power level between about100 Watts to about 200 Watts. In embodiments, pathogens are removed fromsaid insects over a duration of time between about 0.1 seconds to about500 seconds. In embodiments, pathogens are removed from said insectsover a duration of time between about 0.5 seconds to about 15 seconds.In other embodiments, pathogens may be removed by boiling the insects inwater.

FIG. 1A in no way describes every possible embodiment of the pathogenreduction disclosure because describing every possible embodiment wouldbe impractical, if not impossible. FIG. 13 elaborates upon otherpossibilities related to removing pathogens from insects.

Multifunctional Flour Mixing (Step H)

The multifunctional flour mixing (step H) involves mixing the insectswith fiber-starch materials, binding agents, density improving texturalsupplements, moisture improving textural supplements, and optionallycannabis enhancers, to form a multifunctional flour composition. Themultifunctional flour composition may be further processed to createfoodstuffs not only including ada, bagels, baked goods, biscuits,bitterballen, bonda, breads, cakes, candies, cereals, chips, chocolatebars, chocolate, coffee, cokodok, confectionery, cookies, cookingbatter, corn starch mixtures, crackers, crêpes, croissants, croquettes,croutons, dolma, dough, doughnuts, energy bars, flapjacks, french fries,frozen custard, frozen desserts, frying cakes, fudge, gelatin mixes,granola bars, gulha, hardtack, ice cream, khandvi, khanom buang,krumpets, meze, mixed flours, muffins, multi-grain snacks, nachos, niangao, noodles, nougat, onion rings, pakora, pancakes, panforte, pastas,pastries, pie crust, pita chips, pizza, poffertjes, pretzels, proteinpowders, pudding, rice krispie treats, sesame sticks, smoothies, snacks,specialty milk, tele-bhaja, tempura, toffee, tortillas, totopo, turkishdelights, or waffles.

In embodiments, the fiber-starch materials may be comprised of singularor mixtures of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, or vegetable-based materials. In embodiments, thefiber-starch mass ratio ranges from between about 400 pounds offiber-starch per ton of multifunctional flour to about 1800 pounds offiber-starch per ton of multifunctional flour.

In embodiments, the binding agents may be comprised of singular ormixtures of agar, agave, alginin, arrowroot, carrageenan, collagen,cornstarch, egg whites, finely ground seeds, furcellaran, gelatin, guargum, honey, katakuri starch, locust bean gum, pectin, potato starch,proteins, psyllium husks, sago, sugars, syrups, tapioca, vegetable gums,or xanthan gum. In embodiments, the binding agent mass ratio ranges frombetween about 10 pounds of binding agent per ton of multifunctionalflour to about 750 pounds of binding agent per ton of multifunctionalflour.

In embodiments, the density improving textural supplements may becomprised of singular or mixtures of extracted arrowroot starch,extracted corn starch, extracted lentil starch, extracted potato starch,or extracted tapioca starch. In embodiments, the density improvingtextural supplement mass ratio ranges from between about 10 pounds ofdensity improving textural supplement per ton of multifunctional flourto about 1000 pounds of density improving textural supplement per ton ofmultifunctional flour.

In embodiments, the moisture improving textural supplements may becomprised of singular or mixtures of almonds, brazil nuts, cacao,cashews, chestnuts, coconut, filberts, hazelnuts, Indian nuts, macadamianuts, nut butters, nut oils, nut powders, peanuts, pecans, pili nuts,pine nuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tigernuts, and walnuts. In embodiments, the moisture improving texturalsupplement mass ratio ranges from between about 10 pounds of moistureimproving textural supplement per ton of multifunctional flour to about1000 pounds of moisture improving textural supplement per ton ofmultifunctional flour.

In embodiments, a cannabis enhancer may be added to the multifunctionalflour. The cannabis enhancer may be marijuana in a powdered, dried,ground, or decarboxylated form. In embodiments, the cannabis enhancermay be remnants of vaporization, such as substantially fixed carbonfeedstock components. In embodiments, the cannabis enhancer may becomprised of volatile feedstock components and a solvent. Inembodiments, the cannabis enhancer may be comprised of volatilefeedstock components and an alcohol. The cannabis enhancer may becomprised of volatile feedstock components and fixed carbon feedstockcomponents. In embodiments, cannabis enhancer may be comprised ofvolatile feedstock components. In embodiments, cannabis enhancer may becomprised of fixed carbon feedstock components. In embodiments, thecannabis enhancer contains tetrahydrocannabinol (THC) in a mixture ofvolatile feedstock components and fixed carbon feedstock components.

In embodiments, the multifunctional flour ranges from between about 25pounds of cannabis enhancer per ton of multifunctional flour to about1800 pounds of cannabis enhancer per ton of multifunctional flour. Inembodiments, the volatile feedstock component mass ratio ranges frombetween about 500 pounds of volatile feedstock components per ton ofcannabis enhancer to about 2000 pounds of volatile feedstock componentsper ton of cannabis enhancer. In embodiments, the volatile feedstockcomponent mass ratio ranges from between about 500 pounds of volatilefeedstock components per ton of multifunctional flour to about 1750pounds of volatile feedstock components per ton of multifunctionalflour. In embodiments, the fixed carbon feedstock component mass ratioranges from between about 100 pounds of fixed carbon feedstockcomponents per ton of cannabis enhancer to about 1700 pounds of fixedcarbon feedstock components per ton of cannabis enhancer. Inembodiments, the fixed carbon feedstock component mass ratio ranges frombetween about 100 pounds of fixed carbon feedstock components per ton ofmultifunctional flour to about 1600 pounds of fixed carbon feedstockcomponents per ton of multifunctional flour.

Accordingly, I wish to make my intentions clear—and at the same time putpotential competitors on clear public notice. It is my intent that thisportion of the specification especially relating to multifunctionalflour mixing and all claims pertaining thereto receive a liberalconstruction and be interpreted to uphold and not destroy my rights asinventor. It is my intent that the claim terms be construed in acharitable and common-sensical manner, in a manner that encompasses theembodiments disclosed in this and other portions of the specificationand drawings relating to multifunctional flour mixing withoutincorporating unrecited, unnecessary limitations. It is my intent thatthe specification relating to multifunctional flour mixing claim termsbe construed as broadly as practicable while preserving the validity ofthe claims. It is my intent that the claim terms be construed in amanner consistent with the context of the overall claim language andthis portion of the specification along with FIGS. 1B and 12A, withoutimporting extraneous limitations from the specification or other sourcesinto the claims, and without confining the scope of the claims to theexact representations depicted in the specification or drawings in FIGS.1B and 12A. It is also my intent that not each and every term of theclaim be systematically defined and rewritten. Claim terms and phrasesshould be construed only to the extent that it will provide helpful,clarifying guidance to the jury, or to the extent needed to resolve alegitimate, good faith dispute that is material to the questions ofvalidity or infringement. Otherwise, simple claim terms and phrasesshould be presented to the jury without any potentially confusing anddifficult-to-apply definitional construction.

FIG. 1C

FIG. 1C elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence step of lipid extraction (step J).

FIG. 1C shows lipid extraction (step J) downstream of the each of thesteps insect collection (step E), insect grinding (step F), and pathogenremoval (step G).

The lipid extraction (step J) is configured to produce extracted lipids(028) from insects that were previously fed an enhanced feedstock. Inembodiments, the insect fat mass ratio ranges from between about 100pounds of fat per ton of insects produced to about 1800 pounds of fatper ton of insects produced. The egg-laying insects that are presentwithin each feeding chambers, and those that are collected, optionallyground, and optionally exposed to a pathogen removal step areintentionally engineered by feeding an enhanced feedstock to possess awide-ranging fat content ranging from between about 5% to about 90% byweight of insects produced.

In embodiments, the feeding chamber produces insects having fatty acidsincluding palmitoleic acid, linoleic acid, alpha-linoleic acid, oleicacid, gamma-linoleic acid, or stearic acid. The fatty acids of theinsects that are fed the enhanced feedstock are lipids. The extractionand use of lipids has many beneficial applications in society involvingmedicine, nanotechnology, consumer products, and chemical productionwith minimal water, feedstock, and environmental impact.

Palmitoleic acid is used to increase insulin sensitivity by suppressinginflammation, reduce inflammation associated with eczema. It is alsoused in cosmetic products, medical products, and can preserve and treatleather. Linoleic acid is used in oil paints and varnishes and is usedin quick-drying oils. It can be used to reduce acne. It has moistureretentive properties and is used to make lotions and soaps (silky feel).It is an essential fatty acid and an emulsifier. Alpha-Linolenic acid isan essential dietary requirement linked to cardiovascular health. Oleicacid is used in hair dyes and soaps (slippery feel). It is also used asa food additive. It is used to manufacture surfactants, soaps, andplasticizers. It is an emulsifying agent in foods and pharmaceuticals.It can penetrate the skin. It can act as an herbicide, insecticide, andfungicide. It can be used in a metallic soap and with copper to cleanmildew. Gamma-Linolenic acid can help prevent nerve damage. Stearic acidis used in foundation, baby lotions, oils, powders, creams, shavingcream, body and hand cream, cleansers, foot powders, sprays,moisturizers, and soaps (hardness). Stearic acid is a thickener used tomake creams, oil pastels, hard candies, and candles. It is a surfactant.It can be used as a lubricant additive in plasticized PVC compounds toaid processing. It is also used to make metallic soaps.

Rubber grade stearic acid can be used as a mold release lubricant forsintering, pressing ceramic powders, and latex foam. It is also used asa thickener in greases. It can be used as a viscosity modifier for oilextraction. Stearic acid combined with castor oil is used to makesofteners for textile sizing. It can be used as a yarn lubricant.Isopropyl Palmitate is in baby lotion/powder/cream, foot powders andsprays. Glyceryl stearate is in nail products, tonics and dressings,cologne/perfumes, concealers, baby lotion/powder/cream, aftershave.Sorbitan stearate is in blush. TEA-Stearate is in mascara. Stearylalcohol is in hair conditioner, hair straighteners and relaxers, tonicsand dressings (help to style hair). Oleyl alcohol is in hairstraighteners and relaxers, and concealers.

Lipids extracted from insects may also be used in emerging areas ofnanotechnology having uses in many areas covering chemistry,engineering, materials science, physics and biology. In coming years,science will continue to develop and increasingly appreciate sources offatty acids derived from insects. For example, investigators are nowseriously focusing on insect derived fatty acids for use in biomedicalsciences, such as bio-imaging, sensing and diagnosis of pathologies atearly stages, targeted drug delivery, and for use with nano-devices thatinteract with the plasma eukaryotic or even prokaryotic cell membranes.

Herein are disclosed systems and methods for obtaining, in massquantities, commercial scale output of insect based lipids for use in avariety of areas throughout society. In embodiments, the lipidextraction (step J) utilizes a lipid extraction unit to extract lipidsfrom insects. In embodiments, the lipid extraction unit is configured toextract lipids by use of a first immiscible liquid and a secondimmiscible liquid. In embodiments, the first immiscible liquid has afirst density and a first molecular weight, and the second immiscibleliquid has a second density and a second molecular weight. Inembodiments, first density is greater than the second density. Inembodiments, first molecular weight is greater than the second molecularweight. In embodiments, a first immiscible liquid and lipid mixture isformed which is comprised of a lipid portion and a first immiscibleliquid portion. In embodiments, second immiscible liquid and particulatemixture is formed which is comprised of a particulate portion and asecond immiscible liquid portion. In embodiments, the particulateportion is comprised of one or more from the group consisting of insectlegs, and wings, and protein.

FIG. 2

FIG. 2 shows a non-limiting embodiment of an enhanced feedstock mixingmodule (1000) including a feedstock distribution module (1A), mineraldistribution module (1B), vitamin distribution module (1C), polymerdistribution module (1D), water distribution module (1E), and anenhanced feedstock distribution module (1F).

FIG. 2 displays a computer (COMP) that is integral to the InsectProduction Superstructure System (IPSS). The computer (COMP) isconfigured to accept a variety of signals from process variables using avariety of sensors and/or controllers, and then apply advanced processlogic control methodologies, strategies and/or sequences to realizemodulation of actuators and/or valves to effectuate optimal operation ofthe Insect Production Superstructure Systems (IPSS) and its associatedmodules not only including feedstock mixing, feedstock splitting, insectfeeding, insect breeding, insect collection, insect grinding, pathogenremoval, multifunctional flour mixing, and lipid extraction modules. Avariety of signals are sent to and from the computer (COMP) to a varietyof controllers, sensors, valves, motors, actuators, and the likedistributed throughout the entire Insect Production SuperstructureSystem (IPSS).

The computer (COMP) applies the control approach and methodology for theeach and every entire control loop on a continuous basis, a discretebasis, or a hybrid combination of a continuous basis and a discretebasis. Further, a computer may be applied to implement the controlmethodology by utilizing process variables obtained by either acontinuous sensor, a discrete sensor, or a combination of a continuoussensor and a discrete sensor and hold the control action at a constantset-point at that specific control output until a later time when thatcontrol algorithm is executed. The time between successiveinterrogations or application of the control algorithm is applied by thecontrol computer is defined as the control interval. The controlinterval for a continuous sensor is typically shorter than that of adiscrete sensor and based upon commercially available mechanical,electrical, or digital continuous or discrete sensors, the controlinterval or control time can vary from 0.2 milliseconds, to 0.5 seconds,to 1.0 second, to 10 seconds, to 30 seconds, to 1 minute, to 5 minutes,to 10 minutes, to 30 minutes, to 1 hour, to 10 hours, or longer. Theoutput from the control computer is transmitted to a controller device.From application of the control logic, the control computer can send avariety of signals to a variety of controllers.

In embodiments, the signals from controllers or sensors are inputted oroutputted to and from a computer (COMP) by a user or operator via aninput/output interface (I/O) as disclosed in FIG. 2 and many others (notonly including FIGS. 3, 5, 6, 7, 8, 9, 10, 11, 12A, 12B, 13, 14A, 14B,14C, 14D, 14E, 14F, 14G, 14H, 14I, 14J, 15, 16, 17, 18, 19, 20, 21, 22,23, 24, 25, 26, 27A, 27B, 28A, 28B, 29-48). Program and sequencinginstructions may be executed to perform particular computationalfunctions such as automated operation of the valves, actuators,controllers, motors, or the like. In one exemplary embodiment, acomputer (COMP) includes a processor (PROC) coupled to a system memory(MEM) via an input/output interface (I/O). The processor (PROC) may beany suitable processor capable of executing instructions. System memory(MEM) may be configured to store instructions and data accessible byprocessor (PROC). In various embodiments, system memory (MEM) may beimplemented using any suitable memory technology. In all illustratedembodiments, program instructions and data implementing desiredfunctions are shown stored within system memory (MEM) as code (CODE). Inembodiments, the I/O interface (I/O) may be configured to coordinate I/Otraffic between processor (PROC) and system memory (MEM). In someembodiments, the I/O interface (I/O) is configured for a user oroperator to input necessary sequencing protocol into the computer (COMP)for process execution, including sequence timing and repetition of agiven number of states to realize a desired sequence of steps and/orstates. In embodiments, the signals operatively coupled to a controller,valve, actuator, motor, or the like, may be an input value to be enteredinto the computer (COMP) by the I/O interface (I/O).

The system is fully flexible to be tuned, configured, and optimized toprovide an environment for scheduling the appropriate process parametersby programmatically controlling the opening and closing of valves atspecific time intervals, or strategically and systematically opening,closing, turning on, turning off, modulating, controlling, or operatingmotors, valves, or actuators at specific time intervals at specifictimes. In embodiments, a user or operator may define control loops,cycle times, step numbers, and states which may be programmed into thecomputer (COMP) by an operator accessible input/output interface (I/O).

Feedstock Distribution Module (1A)

FIG. 2 displays a feedstock distribution module (1A) including afeedstock tank (1A2) that is configured to accept a feedstock (1A1). Thefeedstock tank (1A2) has an interior (1A3), a feedstock input (1A4), afeedstock conveyor (1A5), and a feedstock conveyor output (1A6). Thefeedstock tank (1A2) accepts a feedstock (1A1) to the interior (1A3) andregulates and controls an engineered amount of feedstock (1A1)downstream to be mixed to form an enhanced feedstock. The feedstockconveyor (1A5) has an integrated feedstock mass sensor (1A7) that isconfigured to input and output a signal (1A8) to the computer (COMP).The feedstock conveyor motor (1A9) has a controller (1A10) that isconfigured to input and output a signal (1A11) to the computer (COMP).The feedstock mass sensor (1A7), feedstock conveyor (1A5), and feedstockconveyor motor (1A9) are coupled so as to permit the conveyance,distribution, or output of a precise flow of feedstock (1A1) via afeedstock transfer line (1A14). A feedstock moisture sensor (1A12A) ispreferably installed on the feedstock transfer line (1A14) and isconfigured to input a signal (1A13A) to the computer (COMP).

In embodiments, the insect feeding chamber may operate at an enhancedfeedstock to insect ratio ranging from between about 1 ton of enhancedfeedstock per ton of insects produced to about 5 tons of enhancedfeedstock per ton of insects produced. In embodiments, about 1 ton ofenhanced feedstock can yield about 1 ton of insects. In embodiments,about 2 tons of enhanced feedstock can yield about 1 ton of insects. Inembodiments, about 3 tons of enhanced feedstock can yield about 1 ton ofinsects. In embodiments, about 4 tons of enhanced feedstock can yieldabout 1 ton of insects. In embodiments, about 5 tons of enhancedfeedstock can yield about 1 ton of insects.

Mineral Distribution Module (1B)

FIG. 2 displays a mineral distribution module (1B) including a mineraltank (1B2) that is configured to accept minerals (1B1). The mineral tank(1B2) has an interior (1B3), a mineral input (1B4), a mineral conveyor(1B5), and a mineral conveyor output (1B6). The mineral tank (1B2)accepts minerals (1B1) to the interior (1B3) and regulates and controlsan engineered amount of minerals (1B1) downstream to be mixed to form anenhanced feedstock. The mineral conveyor (1B5) has an integrated mineralmass sensor (1B7) that is configured to input and output a signal (1B8)to the computer (COMP). The mineral conveyor motor (1B9) has acontroller (1B10) that is configured to input and output a signal (1B11)to the computer (COMP). The mineral mass sensor (1B7), mineral conveyor(1B5), and mineral conveyor motor (1B9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of minerals (1B1)via a mineral transfer line (1B12).

Vitamin Distribution Module (1C)

FIG. 2 displays a vitamin distribution module (1C) including a vitamintank (1C2) that is configured to accept vitamins (1C1). The vitamin tank(1C2) has an interior (1C3), a vitamin input (1C4), a vitamin conveyor(105), and a vitamin conveyor output (106). The vitamin tank (1C2)accepts vitamins (1C1) to the interior (1C3) and regulates and controlsan engineered amount of vitamins (1C1) downstream to be mixed to form anenhanced feedstock. The vitamin conveyor (105) has an integrated vitaminmass sensor (1C7) that is configured to input and output a signal (1C8)to the computer (COMP). The vitamin conveyor motor (1C9) has acontroller (1C10) that is configured to input and output a signal (1C11)to the computer (COMP). The vitamin mass sensor (1C7), vitamin conveyor(105), and vitamin conveyor motor (1C9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of vitamins (1C1)via a vitamin transfer line (1C12).

Polymer Distribution Module (1D)

FIG. 2 displays a polymer distribution module (1D) including a polymertank (1D2) that is configured to accept polymer (1D1). The polymer tank(1D2) has an interior (1D3), a polymer input (1D4), a polymer conveyor(1D5), and a polymer conveyor output (1D6). The polymer tank (1D2)accepts polymer (1D1) to the interior (1D3) and regulates and controlsan engineered amount of polymer (1D1) downstream to be mixed to form anenhanced feedstock. The polymer conveyor (1D5) has an integrated polymermass sensor (1D7) that is configured to input and output a signal (1D8)to the computer (COMP). The polymer conveyor motor (1D9) has acontroller (1D10) that is configured to input and output a signal (1D11)to the computer (COMP). The polymer mass sensor (1D7), polymer conveyor(1D5), and polymer conveyor motor (1D9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of polymer (1D1)via a polymer transfer line (1D12). For the context of this disclosure apolymer (1D1) includes exoskeletons of insects separated from anyplurality of separators (S1, S2, S3) contained within the insectevacuation module (3000). For the context of this disclosure a polymer(1D1) includes chitin having the formula of (C8H13O5N)n which is along-chain polymer of an N-acetylglucosamine, a derivative of glucose,and is found in many places throughout the natural world. Chitin is apolymer and a characteristic component of the cell walls of fungi, theexoskeletons of arthropods such as crustaceans (e.g., crabs, lobstersand shrimps) and insects, the radulae of mollusks, and the beaks andinternal shells of cephalopods, including squid and octopuses and on thescales and other soft tissues of fish and lissamphibians. Where recycleof the exoskeletons from the insect evacuation module (3000) to theinsect feeding module (2000) is not possible the polymer (1D1) includesfish scales, fungi, cephalopod shells, cephalopod beaks, Lissamphibiashells, or keratin. In its pure, unmodified form, chitin is translucent,pliable, resilient, and quite tough.

Water Distribution Module (1E)

FIG. 2 illustrates one non-limiting embodiment of a water distributionmodule (1E) that removes contaminants from water (1E1) prior to mixingto form an enhanced feedstock. A source of water (1E1) is routed througha water input line (1E4) and through a first water treatment unit (1E6)and a second water treatment unit (1E11) and into the interior (1E17) ofa water tank (1E16) where it is then pumped via a water supply pump(1E22), though a water control valve (1E36) and then mixed withfeedstock (1A1), minerals (1B1), vitamins (1C1), and polymer (1D1) toform an enhanced feedstock. In embodiments, enhancers (1E44) may beadded to the interior (1E17) of the water tank (1E16). In embodiments,the enhancers (1E44) may include niacin, taurine, glucuronic acid, malicacid, N-acetyl L tyrosine, L-phenylalanine, caffeine, citicoline, insectgrowth hormones, or steroids, or human growth hormones.

A first water pressure sensor (1E2) is positioned on the water inputline (1E4) and is configured to input a signal (1E3) to the computer(COMP). In embodiments, contaminant-laden water (1E5) is routed throughthe water input line (1E4) and transferred to the first water treatmentunit (1E6) via a first water treatment unit input (1E7). The first watertreatment unit (1E6) has a first water treatment unit input (1E7) and afirst water treatment unit output (1E8) and is configured to removecontaminants from the contaminant-laden water (1E5) to form a stream offirst contaminant-depleted water (1E9) that is outputted via a firstcontaminant-depleted water transfer line (1E10). In embodiments, a firstcontaminant-depleted water (1E9) is routed through the firstcontaminant-depleted water transfer line (1E10) and transferred to thesecond water treatment unit (1E11) via a second water treatment unitinput (1E12). The second water treatment unit (1E11) has a second watertreatment unit input (1E12) and a second water treatment unit output(1E13) and is configured to remove contaminants from the firstcontaminant-depleted water (1E9) to form a stream of secondcontaminant-depleted water (1E14) that is outputted via a secondcontaminant-depleted water transfer line (1E15).

The second contaminant-depleted water transfer line (1E15) is connectedto the water tank (1E16) via a water input (1E18). In embodiments, thesecond contaminant-depleted water transfer line (1E15) has a watersupply valve (1E23) interposed in between the second water treatmentunit (1E11) and the water tank (1E16). In embodiments, the pressure dropacross the water supply valve (1E23) may range from: between about 1pound per square inch to about 5 pound per square inch; between about 5pound per square inch to about 10 pound per square inch; between about10 pound per square inch to about 15 pound per square inch; betweenabout 15 pound per square inch to about 20 pound per square inch;between about 25 pound per square inch to about 30 pound per squareinch; between about 35 pound per square inch to about 40 pound persquare inch; between about 45 pound per square inch to about 50 poundper square inch; between about 55 pound per square inch to about 60pound per square inch; between about 65 pound per square inch to about70 pound per square inch; between about 75 pound per square inch toabout 80 pound per square inch; between about 85 pound per square inchto about 90 pound per square inch; between about 95 pound per squareinch to about 100 pound per square inch; between about 100 pound persquare inch to about 125 pound per square inch; between about 125 poundper square inch to about 150 pound per square inch; or, between about150 pound per square inch to about 200 pound per square inch.

The water supply valve (1E23) has a controller (1E24) that is configuredto input and output a signal (1E25) to the computer (COMP). Inembodiments, a source of water (1E1) may be introduced to the interior(1E17) of the water tank (1E16) via a water supply line (1E19) and waterinput (1E18). The first water treatment unit (1E6) and second watertreatment unit (1E11) are optional because in many areas of the worldthe water quality is suitable for humans and animals to drink andingest.

The water tank (1E16) is equipped with a high-water level sensor (1E26)and a low water level sensor (1E28). The high-water level sensor (1E26)is configured to input a signal (1E27) to the computer (COMP) when thelevel reaches a pre-determined highest most vertical height in the watertank (1E16). The low water level sensor (1E28) is configured to input asignal (1E29) to the computer (COMP) when the level reaches apre-determined lowest most vertical height in the water tank (1E16).

A water supply pump (1E22) is connected to the water output (1E20) ofthe water tank (1E16) via a water discharge line (1E21). The watersupply pump (1E22) is configured to transfer water (1E1) from theinterior (1E17) of the water tank (1E16) to create a pressurized watersupply (1E32) that is routed for mixing to form an enhanced feedstockvia a pressurized water supply line (1E33).

A second water pressure sensor (1E30) is positioned on the discharge ofthe water supply pump (1E22) on the pressurized water supply line(1E33). The second water pressure sensor (1E30) is configured to input asignal (1E31) to the computer (COMP). A water flow sensor (1E34) ispositioned on the discharge of the water supply pump (1E22) on thepressurized water supply line (1E33). The water flow sensor (1E34) isconfigured to input a signal (1E35) to the computer (COMP).

A water control valve (1E36) with an integrated controller (1E37) ispositioned on the discharge of the water supply pump (1E22) on thepressurized water supply line (1E33). The controller (1E37) of the watercontrol valve (1E36) is configured to input and output signal (1E38) tothe computer (COMP). Water (1E1) routed through the water control valve(1E36) is then further routed towards being mixed to form an enhancedfeedstock via a water transfer line (1E41). A water quality sensor(1E42) is positioned on the water transfer line (1E41) and is configuredto input a signal (1E43) to the computer (COMP). A third water pressuresensor (1E39) is positioned on the water transfer line (1E41) and isconfigured to input a signal (1E40) to the computer (COMP).

The pressure drop across the water control valve (1E36) may range from:between about 1 pound per square inch to about 5 pound per square inch;between about 5 pound per square inch to about 10 pound per square inch;between about 10 pound per square inch to about 15 pound per squareinch; between about 15 pound per square inch to about 20 pound persquare inch; between about 25 pound per square inch to about 30 poundper square inch; between about 35 pound per square inch to about 40pound per square inch; between about 45 pound per square inch to about50 pound per square inch; between about 55 pound per square inch toabout 60 pound per square inch; between about 65 pound per square inchto about 70 pound per square inch; between about 75 pound per squareinch to about 80 pound per square inch; between about 85 pound persquare inch to about 90 pound per square inch; between about 95 poundper square inch to about 100 pound per square inch; between about 100pound per square inch to about 125 pound per square inch; between about125 pound per square inch to about 150 pound per square inch; or,between about 150 pound per square inch to about 200 pound per squareinch.

Enhancers (1E44) contained within the interior (1E46) of the enhancertank (1E45) may be routed to the interior (1E17) of the water tank(1E16) via an enhancer transfer line (1E48). The enhancer transfer line(1E48) is connected at one end to the enhancer tank (1E45) via anenhancer tank output (1E47) and at another end to the water tank (1E16)via an enhancer input (1E49). A water enhancer supply valve (1E52) withan integrated controller (1E53) is positioned on the enhancer transferline (1E48) and is configured to input and output a signal (1E54) to thecomputer (COMP). An enhancer flow sensor (1E50) is positioned on theenhancer transfer line (1E48) and is configured to input a signal (1E51)to the computer (COMP).

Feedstock (1A1), minerals (1B1), vitamins (1C1), polymer (1D1), andwater (1E1) are mixed to form an enhanced feedstock that is routed tothe interior (1F2) of the enhanced feedstock splitter (1F1) via anenhanced feedstock transfer line (1F0).

In embodiments, water may be added to the enhanced feedstock andtransferred to the feeding chamber so that the insect feeding chamberoperates at a water to insect ratio ranging from: between about 0.1 tonsof water per ton of insects produced to about 0.2 tons of water per tonof insects produced; between about 0.2 tons of water per ton of insectsproduced to about 0.4 tons of water per ton of insects produced; betweenabout 0.4 tons of water per ton of insects produced to about 0.6 tons ofwater per ton of insects produced; between about 0.6 tons of water perton of insects produced to about 0.8 tons of water per ton of insectsproduced; between about 0.8 tons of water per ton of insects produced toabout 1 ton of water per ton of insects produced; between about 1 ton ofwater per ton of insects produced to about 1.5 tons of water per ton ofinsects produced; between about 1.5 tons of water per ton of insectsproduced to about 2 tons of water per ton of insects produced; betweenabout 2 tons of water per ton of insects produced to about 3 tons ofwater per ton of insects produced; between about 3 tons of water per tonof insects produced to about 4 tons of water per ton of insectsproduced; between about 4 tons of water per ton of insects produced toabout 5 tons of water per ton of insects produced; between about 5 tonsof water per ton of insects produced to about 6 tons of water per ton ofinsects produced; between about 6 tons of water per ton of insectsproduced to about 7 tons of water per ton of insects produced; betweenabout 7 tons of water per ton of insects produced to about 8 tons ofwater per ton of insects produced; between about 8 tons of water per tonof insects produced to about 9 tons of water per ton of insectsproduced; between about 9 tons of water per ton of insects produced toabout 10 tons of water per ton of insects produced; between about 10tons of water per ton of insects produced to about 11 tons of water perton of insects produced; between about 11 tons of water per ton ofinsects produced to about 12 tons of water per ton of insects produced;between about 12 tons of water per ton of insects produced to about 13tons of water per ton of insects produced; between about 13 tons ofwater per ton of insects produced to about 14 tons of water per ton ofinsects produced; between about 14 tons of water per ton of insectsproduced to about 15 tons of water per ton of insects produced; betweenabout 15 tons of water per ton of insects produced to about 16 tons ofwater per ton of insects produced; between about 16 tons of water perton of insects produced to about 17 tons of water per ton of insectsproduced; between about 17 tons of water per ton of insects produced toabout 18 tons of water per ton of insects produced; between about 18tons of water per ton of insects produced to about 19 tons of water perton of insects produced; or, between about 19 tons of water per ton ofinsects produced to about 20 tons of water per ton of insects produced.

In embodiments, about 0.1 tons of water yields 1 ton of insects. Inembodiments, about 0.2 tons of water yields 1 ton of insects. Inembodiments, about 0.4 tons of water yields 1 ton of insects. Inembodiments, about 0.6 tons of water yields 1 ton of insects. Inembodiments, about 0.8 tons of water yields 1 ton of insects. Inembodiments, about 1 ton of water yields 1 ton of insects. Inembodiments, about 2 tons of water yields 1 ton of insects. Inembodiments, about 3 tons of water yields 1 ton of insects. Inembodiments, about 4 tons of water yields 1 ton of insects. Inembodiments, about 5 tons of water yields 1 ton of insects. Inembodiments, about 6 tons of water yields 1 ton of insects. Inembodiments, about 7 tons of water yields 1 ton of insects. Inembodiments, about 8 tons of water yields 1 ton of insects. Inembodiments, about 9 tons of water yields 1 ton of insects. Inembodiments, about 10 tons of water yields 1 ton of insects. Inembodiments, about 11 tons of water yields 1 ton of insects. Inembodiments, about 12 tons of water yields 1 ton of insects. Inembodiments, about 13 tons of water yields 1 ton of insects. Inembodiments, about 14 tons of water yields 1 ton of insects. Inembodiments, about 15 tons of water yields 1 ton of insects. Inembodiments, about 16 tons of water yields 1 ton of insects. Inembodiments, about 17 tons of water yields 1 ton of insects. Inembodiments, about 18 tons of water yields 1 ton of insects. Inembodiments, about 19 tons of water yields 1 ton of insects. Inembodiments, about 20 tons of water yields 1 ton of insects.

Enhanced Feedstock Distribution Module (1F)

The enhanced feedstock splitter (1F1) has an interior (1F2), a splitterinput (1F3), a first output (1F10), second output (1F15), and a thirdoutput (1F20). The enhanced feedstock splitter (1F1) is configured tomix the feedstock (1A1), minerals (1B1), vitamins (1C1), polymer (1D1),and water (1E1) and to split the mixed enhanced feedstock into aplurality of streams including a first enhanced feedstock stream (EF1),second enhanced feedstock stream (EF2), and a third enhanced feedstockstream (EF3). Each of the first enhanced feedstock stream (EF1), secondenhanced feedstock stream (EF2), and third enhanced feedstock stream(EF3), may be transferred each to a first feeding chamber (FC1), secondfeeding chamber (FC2), and third feeding chamber (FC3), respectively.

An enhanced feedstock moisture sensor (1A12B) is positioned on theenhanced feedstock transfer line (1F0) and is configured to input asignal (1A13B) to the computer (COMP). The enhanced feedstock moisturesensor (1A12B) may be used to gauge the amount of moisture within theenhanced feedstock to increase or decrease the flow of water (1E1)passed through the water flow sensor (1E34) and water control valve(1E36).

The enhanced feedstock splitter (1F1) has a top section (1F4), bottomsection (1F5), and at least one side wall (1F6). The enhanced feedstocksplitter (1F1) may be cylindrical or rectangular or any otherconceivable shape so long as it outputs at least one first enhancedfeedstock stream. In embodiments, the enhanced feedstock splitter (1F1)has a splitter input (1F3) positioned on the top section (1F4).

In embodiments, the enhanced feedstock splitter (1F1) has a splitterfirst screw conveyor (1F9), splitter second screw conveyor (1F14), andsplitter third screw conveyor (1F19) positioned on the bottom section(1F5). In embodiments, a first splitter level sensor (1F7) is positionedon the side wall (1F6) of the enhanced feedstock splitter (1F1) which isconfigured to input a signal (1F8) to the computer (COMP).

The splitter first screw conveyor (1F9) has a first output (1F10) and isconfigured to discharge a first enhanced feedstock stream (EF1) to afirst feeding chamber (FC1). The splitter first screw conveyor (1F9) isequipped with a splitter first screw conveyor motor (1F11) andintegrated controller (1F12) that is configured to input and output asignal (1F13) to the computer (COMP).

A first weigh screw (1F24) is positioned on the first output (1F10) ofthe splitter first screw conveyor (1F9). The first weigh screw (1F24)has a first weigh screw input (1F25) and a first weigh screw output(1F26), with an integrated mass sensor (1F27) that is configured toinput a signal (1F28) to the computer (COMP). The first weigh screw(1F24) has a first weigh screw motor (1F29) with an integratedcontroller (1F30) that is configured to input and output a signal (1F31)to the computer (COMP). A first weighed enhanced feedstock stream (1F32)or a first enhanced feedstock stream (EF1) is discharged from the firstweigh screw output (1F26).

The splitter second screw conveyor (1F14) has a first output (1F10) andis configured to discharge a second enhanced feedstock stream (EF2) to asecond feeding chamber (FC2). The splitter second screw conveyor (1F14)is equipped with a splitter second screw conveyor motor (1F16) andintegrated controller (1F17) that is configured to input and output asignal (1F18) to the computer (COMP). A second weigh screw (1F33) ispositioned on the second output (1F15) of the splitter second screwconveyor (1F14). The second weigh screw (1F33) has a second weigh screwinput (1F34) and a second weigh screw output (1F35), with an integratedmass sensor (1F26) that is configured to input a signal (1F37) to thecomputer (COMP). The second weigh screw (1F33) has a second weigh screwmotor (1F38) with an integrated controller (1F39) that is configured toinput and output a signal (1F40) to the computer (COMP). A secondweighed enhanced feedstock stream (1F41) or a second enhanced feedstockstream (EF2) is discharged from the second weigh screw output (1F35).

The splitter third screw conveyor (1F19) has a first output (1F10) andis configured to third enhanced feedstock stream (EF3) to a thirdfeeding chamber (FC3). The splitter third screw conveyor (1F19) isequipped with a splitter third screw conveyor motor (1F21) andintegrated controller (1F22) that is configured to input and output asignal (1F23) to the computer (COMP). A third weigh screw (1F42) ispositioned on the third output (1F20) of the splitter third screwconveyor (1F19). The third weigh screw (1F42) has a third weigh screwinput (1F43) and a third weigh screw output (1F44), with an integratedmass sensor (1F45) that is configured to input a signal (1F46) to thecomputer (COMP). The third weigh screw (1F42) has a third weigh screwmotor (1F47) with an integrated controller (1F48) that is configured toinput and output a signal (1F49) to the computer (COMP). A third weighedenhanced feedstock stream (1F50) or a third enhanced feedstock stream(EF3) is discharged from the third weigh screw output (1F44).

FIG. 3

FIG. 3 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein the egg transfer system (244) of theinsect feeding module (2000) is at a first state in a first retractedheight (H1).

A first weighed enhanced feedstock stream (1F32), or otherwise termed afirst enhanced feedstock stream (EF1), is shown in FIG. 3 to beintroduced to a first feeding chamber (FC1) of an insect feeding module(2000) via an enhanced feedstock input (206). The non-limitingdescription of the insect feeding module (2000) shown in FIG. 3 includesa feeding chamber (200). In embodiments, the feeding chamber (200) inFIG. 3 is a first feeding chamber (FC1) in an Insect ProductionSuperstructure System (IPSS) that includes a plurality of insect feedingchambers (FC1, FC2, FC3). The insect feeding module (2000) is shown tobe in fluid communication with an insect evacuation module (3000). Thefeeding chamber (200) contained within an insect feeding module (2000)of FIG. 3 is shown to be in fluid communication with a separator (300)contained within an insect evacuation module (3000).

The feeding chamber (200) of is shown to have an interior (201) definedby at least one side wall (202). Each side wall (202) of the embodimentof FIG. 3 is shown to have perforations as to be comprised of a mesh, ora screen, or the like. However, it is to be noted that any such wall,perforated or not perforated, screen or an impermeable surface shallsuffice. It is also to be noted that the side wall (202) when made up ofa screen-type material has opening that are lesser in size than theinsects contained within the interior (201) of the feeding chamber(200).

In embodiments, the feeding chamber (200) has both a top (203) and abottom (204). In the embodiment of FIG. 3, the top and bottom are bothmade up of a permeable metal or plastic or wire mesh or the like.However, in some embodiments, there is no bottom (204) at all, or thebottom is made up of a plurality of slats as described below. The firstweighed enhanced feedstock stream (1F32), or otherwise termed a firstenhanced feedstock stream (EF1), is introduced to an enhanced feedstockdistributor (207) positioned within the interior (201) of the feedingchamber (200).

The feeding chamber is equipped with a humidity sensor (208) that isconfigured to measure the humidity within the interior (201) and input asignal (209) to the computer (COMP). The feeding chamber is equippedwith a first temperature sensor (210) that is configured to measure thetemperature of a first region within the interior (201) and input asignal (211) to the computer (COMP). The feeding chamber is equippedwith a second temperature sensor (212) that is configured to measure thetemperature of a first region within the interior (201) and input asignal (213) to the computer (COMP).

A network (220) of cells (219) are positioned within the interior (201)of the feeding chamber and are configured to permit insects (225) toreside therein. FIG. 4 shows one non-limiting embodiment of a network(220) of cells (219) for growing insects within a feeding chamber (200)of the insect feeding module (2000) shown in FIG. 3. The network (220)of cells (219) has openings (222) positioned at a first end (221) andopenings (224) positioned at a second end (223). Insects (225) mayreside in the passageways between the openings (222) at the first end(221) and the openings (224) at the second end (223). The cells (219)have a cell length (C-L) and a cell width (C-W). The network (220) ofcells (219) has a network length (N-L) and a network width (N-W). Inembodiments, the network (220) of cells (219) has a network length (N-L)that is greater than the network width (N-W). In embodiments, thenetwork (220) of cells (219) has a network length (N-L) that is lessthan the network width (N-W). The cell width (C-W) is greater than thewidth (1 i-W) of a first insect (1 i) that resides within the interior(201) of the feeding chamber (200). The cell width (C-W) is greater thanthe average insect width (Ni-W) of a Nth insect (Ni) that collectivelyreside within the interior (201) of the feeding chamber (200). The celllength (C-L) is greater than the length (2 i-L) of a first insect (1 i)that resides within the interior (201) of the feeding chamber (200). Thecell length (C-L) is greater than the average insect length (Ni-LW) of aNth insect (Ni) that collectively reside within the interior (201) ofthe feeding chamber (200).

Obviously, many insects (225) may be present within the feeding chamber(200) at any given time.

This may include: a first insect (1 i) having a first insect length (1i-L), a first insect width (1 i-W), and a first insect mass (1 i-WT); asecond insect (2 i) having a second insect length (2 i-L), a secondinsect width (2 i-W), and a second insect mass (2 i-WT); and a Nthinsect (Ni) that has an average insect length (Ni-L), an average insectwidth (Ni-W), and an average insect mass (Ni-WT). The average insectlength (Ni-L) is the sum of the first insect length (1 i-L) and thesecond insect length (2 i-L) divided by the number of insects that beingtwo in this particular instance and embodiment. The average insect width(Ni-W) is the sum of the first insect width (1 i-W) and the secondinsect width (2 i-W) divided by the number of insects that being two inthis particular instance and embodiment. It is of course obvious to oneof ordinary skill in the art that more than two insects (225, 1 i, 2 i)are contained within the interior (201) of the feeding chamber (200) andthat both the average insect length (Ni-L) and average insect width(Ni-W) are averaged over a plurality of insects.

In embodiments, the cell width (C-W) ranges from: between about 0.125inches to about 0.25 inches; between about 0.25 inches to about 0.50inches; between about 0.5 inches to about 0.75 inches; between about0.75 inches to about 1 inch; between about 1 inch to about 1.25 inches;between about 1.25 inch to about 1.50 inches; between about 1.50 inchesto about 1.75 inches; between about 1.75 inches to about 2 inches;between about 2 inches to about 2.25 inches; between about 2.25 inchesto about 2.50 inches; between about 2.50 inches to about 2.75 inches;between about 2.75 inches to about 2.75 inches; between about 2.75inches to about 3 inches; between about 3 inches to about 3.25 inches;between about 3.25 inch to about 3.50 inches; between about 3.50 inchesto about 3.75 inches; between about 3.75 inches to about 4 inches;between about 4 inches to about 4.25 inches; between about 4.25 inch toabout 4.50 inches; between about 4.50 inches to about 4.75 inches; and,between about 4.75 inches to about 5 inches.

In embodiments, the cell length (C-L) ranges from: between about 0.5feet to about 1 foot; between about 1 feet to about 2 feet; betweenabout 2 feet to about 3 feet; between about 3 feet to about 4 feet;between about 4 feet to about 5 feet; between about 5 feet to about 6feet; between about 6 feet to about 7 feet; between about 7 feet toabout 8 feet; between about 8 feet to about 9 feet; between about 9 feetto about 10 feet; between about 10 feet to about 11 feet; between about11 feet to about 12 feet; between about 12 feet to about 13 feet;between about 13 feet to about 14 feet; between about 14 feet to about15 feet; between about 15 feet to about 16 feet; between about 16 feetto about 17 feet; between about 17 feet to about 18 feet; between about18 feet to about 19 feet; between about 19 feet to about 20 feet;between about 20 feet to about 21 feet; between about 21 feet to about22 feet; between about 22 feet to about 23 feet; between about 23 feetto about 24 feet; between about 24 feet to about 25 feet; between about25 feet to about 26 feet; between about 26 feet to about 27 feet;between about 27 feet to about 28 feet; between about 28 feet to about29 feet; between about 29 feet to about 30 feet; between about 30 feetto about 31 feet; between about 31 feet to about 32 feet; between about32 feet to about 33 feet; between about 33 feet to about 34 feet;between about 34 feet to about 35 feet; between about 35 feet to about36 feet; between about 36 feet to about 37 feet; between about 37 feetto about 38 feet; between about 38 feet to about 39 feet; and, betweenabout 39 feet to about 40 feet.

In embodiments, the average insect width (Ni-W) ranges from: betweenabout 0.015625 inches to about 0.03125 inches; between about 0.03125inches to about 0.0625 inches; between about 0.0625 inches to about0.125 inches; between about 0.125 inches to about 0.25 inches; betweenabout 0.25 inches to about 0.50 inches; between about 0.5 inches toabout 0.75 inches; between about 0.75 inches to about 1 inch; betweenabout 1 inch to about 1.25 inches; between about 1.25 inch to about 1.50inches; between about 1.50 inches to about 1.75 inches; between about1.75 inches to about 2 inches; between about 2 inches to about 2.25inches; between about 2.25 inches to about 2.50 inches; between about2.50 inches to about 2.75 inches; between about 2.75 inches to about2.75 inches; and, between about 2.75 inches to about 3 inches.

In embodiments, the average insect length (Ni-L) ranges from: betweenabout 0.125 inches to about 0.25 inches; between about 0.25 inches toabout 0.50 inches; between about 0.5 inches to about 0.75 inches;between about 0.75 inches to about 1 inch; between about 1 inch to about1.25 inches; between about 1.25 inch to about 1.50 inches; between about1.50 inches to about 1.75 inches; between about 1.75 inches to about 2inches; between about 2 inches to about 2.25 inches; between about 2.25inches to about 2.50 inches; between about 2.50 inches to about 2.75inches; between about 2.75 inches to about 2.75 inches; between about2.75 inches to about 3 inches; between about 3 inches to about 3.25inches; between about 3.25 inch to about 3.50 inches; between about 3.50inches to about 3.75 inches; between about 3.75 inches to about 4inches; between about 4 inches to about 4.25 inches; between about 4.25inch to about 4.50 inches; between about 4.50 inches to about 4.75inches; between about 4.75 inches to about 5 inches; between about 5inches to about 5.25 inches; between about 5.25 inches to about 5.5inches; between about 5.5 inches to about 5.75 inches; between about5.75 inches to about 6 inches; between about 6 inches to about 7 inches;between about 7 inches to about 8 inches; between about 8 inches toabout 9 inches; and, between about 9 inches to about 10 inches.

Referring again to FIG. 3, a vibration unit (214) may be connected tothe network (220) of cells (219) at a first vibration unit connection(218A) and a second vibration unit connection (218B). The vibration unit(214) is equipped with a vibration unit motor (215) and integratedcontroller (216) that is configured to input and output a signal (217)to the computer (COMP). The vibration unit (214) is used to shake or toprovide oscillations to occur within the network (220) of cells (219) todislodge insects (225) from within the passageway between the first end(221) openings (222) and the second end (223) openings (224).Alternately, the vibration unit (214) may vibrate the entire feedingchamber (200) or at least a portion of the feeding chamber (200) so asto effectuate disclosing insects (225) from their resting surface withinthe network (220) of cells (219) in between the first end (221) openings(222) and the second end (223) openings (224).

In embodiments, a cell network differential pressure sensor (226) may beinstalled to measure to pressure across the network (220) of cells (219)to ascertain some measure of the mass or volume or quantity of insectsthat reside in between the first end (221) openings (222) and the secondend (223) openings (224).

The cell network differential pressure sensor (226) is configured toinput a signal (227) to the computer (COMP). When a pre-determineddifferential pressure is measured across the feeding chamber (200),insects may be evacuated therefrom. In embodiments, the pre-determineddifferential pressure across the feeding chamber (200) ranges from:about 0.015625 inches of water to about 0.03125 inches of water; betweenabout 0.03125 inches of water to about 0.0625 inches of water; betweenabout 0.0625 inches of water to about 0.125 inches of water; betweenabout 0.125 inches of water to about 0.25 inches of water; between about0.25 inches of water to about 0.50 inches of water; between about 0.5inches of water to about 0.75 inches of water; between about 0.75 inchesof water to about 1 inch; between about 1 inch to about 1.25 inches ofwater; between about 1.25 inch to about 1.50 inches of water; betweenabout 1.50 inches of water to about 1.75 inches of water; between about1.75 inches of water to about 2 inches of water; between about 2 inchesof water to about 2.25 inches of water; between about 2.25 inches ofwater to about 2.50 inches of water; between about 2.50 inches of waterto about 2.75 inches of water; between about 2.75 inches of water toabout 2.75 inches of water; between about 2.75 inches of water to about3 inches of water; between about 3 inches of water to about 3.25 inchesof water; between about 3.25 inch to about 3.50 inches of water; betweenabout 3.50 inches of water to about 3.75 inches of water; between about3.75 inches of water to about 4 inches of water; between about 4 inchesof water to about 4.25 inches of water; between about 4.25 inch to about4.50 inches of water; between about 4.50 inches of water to about 4.75inches of water; between about 4.75 inches of water to about 5 inches ofwater; between about 5 inches of water to about 5.25 inches of water;between about 5.25 inches of water to about 5.5 inches of water; betweenabout 5.5 inches of water to about 5.75 inches of water; between about5.75 inches of water to about 6 inches of water; between about 6 inchesof water to about 7 inches of water; between about 7 inches of water toabout 8 inches of water; between about 8 inches of water to about 9inches of water; between about 10 inches of water to about 15 inches ofwater; between about 15 inches of water to about 20 inches of water;between about 20 inches of water to about 25 inches of water; betweenabout 25 inches of water to about 30 inches of water; between about 30inches of water to about 35 inches of water; between about 35 inches ofwater to about 40 inches of water; between about 40 inches of water toabout 45 inches of water; between about 45 inches of water to about 50inches of water; between about 50 inches of water to about 55 inches ofwater; between about 55 inches of water to about 60 inches of water;between about 60 inches of water to about 65 inches of water; betweenabout 65 inches of water to about 70 inches of water; between about 70inches of water to about 75 inches of water; between about 75 inches ofwater to about 80 inches of water; between about 80 inches of water toabout 85 inches of water; between about 85 inches of water to about 90inches of water; between about 90 inches of water to about 95 inches ofwater; and, between about 95 inches of water to about 100 inches ofwater.

The cell network differential pressure sensor (226) is connected to theinterior (201) of the feeding chamber (200) by a first end impulse line(228) with a first end impulse line connection (232) and a second endimpulse line (233) with a second end impulse line connection (237). FIG.3 shows the first end impulse line (228) connected to the feedingchamber (200) via a first end impulse line connection (232) that ispositioned vertically above the first end (221) openings (222) of thenetwork (220) of cells (219). FIG. 3 also shows the second end impulseline (233) connected to the feeding chamber (200) via a second endimpulse line connection (237) that is positioned vertically below thesecond end (223) openings (224) of the network (220) of cells (219).

The first end impulse line (228) and second end impulse line (233) arepreferably tubes ranging from ⅛″, ¼″, ⅜″, ½″, ¾″, or 1″ stainless steel,plastic, polymer, metal tubing or piping. To prevent insects (225) fromcrawling up the first end impulse line (228), or to prevent clogging ofparticulates, and thus preventing the cell network differential pressuresensor (226) from accurately measuring differential pressure across thenetwork (220) of cells (219), a first impulse line gas supply (231) maybe provided to apply a continuous purge or gas, such as air, or CO2, orthe like. The first impulse line gas supply (231) is controlled and setto a pre-determined flow rate by adjusting a first air purge flowregulator (230) wherein the flow rate is detected via a first air purgeflow sensor (229). Similarly, to prevent insects (225) from crawling upthe second end impulse line (233), or to prevent clogging ofparticulates, and thus preventing the cell network differential pressuresensor (226) from accurately measuring differential pressure across thenetwork (220) of cells (219), a second impulse line gas supply (236) maybe provided to apply a continuous purge or gas, such as air, or CO2, orthe like. The second impulse line gas supply (236) is controlled and setto a pre-determined flow rate by adjusting a second air purge flowregulator (235) wherein the flow rate is detected via a second air purgeflow sensor (234).

An air input (260) is configured to permit an air supply (262) to betransferred to the interior (201) of the feeding chamber (200) via anair supply entry conduit (261). An optional inlet gas distributor (263)may be positioned at the interface of the air input (260) so as tosubstantially uniformly distribute the air supply (262) over thecross-section of the interior (201) of the feeding chamber (200). Inembodiments, the inlet gas distributor (263) may serve to effectuate ahigh velocity blast of air to the openings (222, 224) of the network(220) of cells (219) to aide in dislodging insects (225) from the cells(219) and to permit substantially complete evacuation of the egg-layinginsects (225) present thing the interior (201) of the feeding chamber(200).

FIG. 3 shows an air supply fan (271) connected to the interior (201) ofthe feeding chamber (200) via the air supply entry conduit (261). Theair supply fan (271) equipped with an air supply fan motor (272) andcontroller (273) is configured to input and output a signal (274) to thecomputer (COMP). An air heater (264) may be interposed in the air supplyentry conduit (261) in between the air supply fan (271) and the feedingchamber (200).

Water (275) in the form of liquid or vapor may be introduced to the airsupply entry conduit (261) via a water transfer line (276). A waterinput valve (278), and a water flow sensor (279) may also be installedon the water transfer line (276). The water flow sensor (279) isconfigured to input a signal (280) to the computer (COMP). The airsupply (262) may be mixed with the water (275) in a water and gas mixingsection (281) of the air supply entry conduit (261). FIG. 1 shows thewater and gas mixing section (281) upstream of the air heater (264) butit may alternately also be placed downstream.

The air heater (264) may be electric, operated by natural gas,combustion, solar energy, alternative energy, or it may be a heattransfer device that uses a working heat transfer medium, such as steamor any other heat transfer medium known to persons having an ordinaryskill in the art to which it pertains. FIG. 3 shows the air heater (264)to have a heat transfer medium input (265) and a heat transfer mediumoutput (266).

In embodiments, heat transfer medium input (265) of the air heater (264)is equipped with a heat exchanger heat transfer medium inlet temperature(T3) that is configured to input a signal (XT3) to the computer (COMP).In embodiments, heat transfer medium output (266) of the air heater(264) is equipped with a heat exchanger heat transfer medium outlettemperature (T4) that is configured to input a signal (XT4) to thecomputer (COMP).

A first humidity sensor (267) is positioned on the discharge of the airsupply fan (271) upstream of the water and gas mixing section (281). Thefirst humidity sensor (267) is configured to input a signal (268) to thecomputer (COMP). A heat exchanger inlet gas temperature sensor (T1) ispositioned on the discharge of the air supply fan (271) upstream of theair heater (264). The heat exchanger inlet gas temperature sensor (T1)is configured to input a signal (XT1) to the computer (COMP).

A second humidity sensor (269) is positioned on the discharge of the airheater (264) upstream of the air input (260) to the interior (201) ofthe feeding chamber (200). The second humidity sensor (266) isconfigured to input a signal (270) to the computer (COMP). A heatexchanger outlet gas temperature sensor (T2) is positioned on thedischarge of the air heater (264) upstream of the air input (260) to theinterior (201) of the feeding chamber (200). The heat exchanger outletgas temperature sensor (T2) is configured to input a signal (XT2) to thecomputer (COMP).

In embodiments, the air supply fan (271), air heater (264), and airsupply (262), permit the computer automation while integrated with theheat exchanger inlet gas temperature sensor (T1), heat exchanger outletgas temperature sensor (T2), and feeding chamber (200) temperaturesensors (210, 212), to operate under a wide variety of automatedtemperature operating conditions including varying the temperature rangein the feeding chamber (200) from: below 32 degrees Fahrenheit, betweenabout 32 degrees Fahrenheit to about 40 degrees Fahrenheit; betweenabout 40 degrees Fahrenheit to about 45 degrees Fahrenheit; betweenabout 45 degrees Fahrenheit to about 50 degrees Fahrenheit; betweenabout 50 degrees Fahrenheit to about 55 degrees Fahrenheit; betweenabout 55 degrees Fahrenheit to about 60 degrees Fahrenheit; betweenabout 60 degrees Fahrenheit to about 65 degrees Fahrenheit; betweenabout 65 degrees Fahrenheit to about 70 degrees Fahrenheit; betweenabout 70 degrees Fahrenheit to about 75 degrees Fahrenheit; betweenabout 75 degrees Fahrenheit to about 80 degrees Fahrenheit; betweenabout 80 degrees Fahrenheit to about 85 degrees Fahrenheit; betweenabout 85 degrees Fahrenheit to about 90 degrees Fahrenheit; betweenabout 90 degrees Fahrenheit to about 95 degrees Fahrenheit; betweenabout 95 degrees Fahrenheit to about 100 degrees Fahrenheit; betweenabout 100 degrees Fahrenheit to about 105 degrees Fahrenheit; betweenabout 105 degrees Fahrenheit to about 110 degrees Fahrenheit; betweenabout 110 degrees Fahrenheit to about 115 degrees Fahrenheit; and,between about 115 degrees Fahrenheit to about 120 degrees Fahrenheit.

In embodiments, the air supply fan (271), air heater (264), air supply(262), and water (275) permit the computer automation while integratedwith the first humidity sensor (267), second humidity sensor (269), andfeeding chamber (200) humidity sensor (208), to operate under a widevariety of automated operating humidity conditions including varying thehumidity range in the feeding chamber (200) from: between about 5percent humidity to about 10 percent humidity; between about 10 percenthumidity to about 15 percent humidity; between about 15 percent humidityto about 20 percent humidity; between about 20 percent humidity to about25 percent humidity; between about 25 percent humidity to about 30percent humidity; between about 30 percent humidity to about 35 percenthumidity; between about 35 percent humidity to about 40 percenthumidity; between about 40 percent humidity to about 45 percenthumidity; between about 45 percent humidity to about 50 percenthumidity; between about 50 percent humidity to about 55 percenthumidity; between about 55 percent humidity to about 60 percenthumidity; between about 60 percent humidity to about 65 percenthumidity; between about 65 percent humidity to about 70 percenthumidity; between about 70 percent humidity to about 75 percenthumidity; between about 75 percent humidity to about 80 percenthumidity; between about 80 percent humidity to about 85 percenthumidity; between about 85 percent humidity to about 90 percenthumidity; between about 90 percent humidity to about 95 percenthumidity; and, between about 95 percent humidity to about 100 percenthumidity.

FIG. 3 shows the feeding chamber (200) connected to a separator (300)via a feeding chamber exit conduit (302). The insect evacuation module(3000) shown in FIG. 3 only contains a first separator (S1), however itis to be noted that more than one separator (S2, S3) may be utilized insome circumstances.

The feeding chamber exit conduit (302) is connected at a first end tothe feeding chamber (200) via an insect evacuation output (205) andconnected at another end to a separator (300) via an insect and gasmixture input (303). The feeding chamber exit conduit (302) isconfigured to transfer an insect and gas mixture (304) from the feedingchamber (200) to the separator (300).

The insect and gas mixture (304) has an insect portion (304A) and a gasportion (304B). The gas portion is mostly air, however may contain someCO2 if some CO2 is used in the first impulse line gas supply (231) orthe second impulse line gas supply (236). The separator (300), showingin FIG. 3 as a first separator (S1), is also shown in a filter. However,in other embodiments, the first separator (S1) may be a filter, acyclone, or any other conceivable means to achieve the end of separatinginsects from a gas.

The separator (300) of FIG. 3 is a filter and contains an interior(301), an entry section (305) and an exit section (307). A filterelement (306) separates the entry section (305) from the exit section(307) so as to only permit the gas portion (304B) of the insect and gasmixture (304) to flow through the filter element (306) from the entrysection (305) to the exit section (307).

The insect portion (304A) of the insect and gas mixture (304) isretained within the entry section (305) because the pores or openings inthe filter element (306) are smaller than the average insect length(Ni-L) or the average insect width (Ni-W) of the insects (225, Ni)contained within the interior (201) of the feeding chamber (200) andtransferred to the separator (300).

A differential pressure sensor (308) is installed on the separator (300)to measure the pressure drop across the filter element (306) in betweenthe entry section (305) and exit section (307). The differentialpressure sensor (308) is configured to input a signal (309) to thecomputer (COMP). The differential pressure sensor (308) has an entrysection impulse line (310) in fluid communication with the entry section(305) as well as an exit section impulse line (311) in fluidcommunication with the exit section (307).

An insect evacuation fan (312) pulls a vacuum through the separator(300, S1) and in turn pulls a vacuum on the feeding chamber (200). Theinsect evacuation fan (312) is configured to pull a vacuum on thefeeding chamber to remove insects (225) from within the network (220) ofcells 219). Specifically, the insect evacuation fan (312) pulls a vacuumon the network (220) of cells (219) and sucks insects from the inbetween the openings (222) of the first end (221) and the openings (224)of the second end (223) so as to substantially completely evacuateegg-laying insects (225) from the interior (201) of the feeding chamber(200).

When a vacuum is pulled on the feeding chamber the cell networkdifferential pressure sensor (226) sends a signal (227) to the computer(COMP) so as to quantify the quantity of mass of insects (225) presentwithin the network (220) of cells (219) within the feeding chamber (200)interior (201).

The insect evacuation fan (312) is equipped with a fan motor (314) and acontroller (316) that is configured to input and output a signal (318)to the computer (COMP). The insect evacuation fan (312) is connected tothe separator (300) via an insect-depleted gas output (321). Theinsect-depleted gas output (321) is configured to transfer aninsect-depleted gas (320) from the separator (300) to the inlet of theinsect evacuation fan (312). The insect-depleted gas (320) has a reducedamount of insects in it in reference to the insect and gas mixture(304). The insect evacuation fan (312) discharges the insect-depletedgas (320) via an insect-depleted gas exhaust line (322). A portion ofthe insect-depleted gas (320) that passes through the insect-depletedgas exhaust line (322) may be routed back to the separator to backflushthe filter element (306). Thus, the insect-depleted gas exhaust line(322) is in fluid communication with the separator (300) via aninsect-depleted gas recycle line (323) and an exhaust gas recycle input(324).

The separator (300) may be equipped with a valve (325) with a controller(326) that is configured to input a signal (327) to the computer (COMP).The valve (325) is preferably a rotary style valve, but may in someembodiments be that of a ball valve, butterfly valve, knife valve,piston valve, or plug valve.

The separator (300) may also be equipped with a separated insectconveyor (328) to remove separated insects (334) from the separator(300). The separated insect conveyor (328) has a motor (329) and acontroller (330) that is configured to input and output a signal (331)to the computer (COMP). The separated insect conveyor (328) may also beequipped with a mass sensor (332) for weighing the separated insects(334) by sending a signal (333) to the computer (COMP). The separatedinsect conveyor (328) may be any type of conveyor, but preferably is ascrew auger. Other types of conveyors are compression screw conveyors,conveyor belts, a pneumatic conveyor system, a vibrating conveyorsystem, a flexible conveyor system, a vertical conveyor system, a spiralconveyor system, a drag chain conveyor system, or a heavy duty rearconveyor system. Any conceivable type of mechanical handling equipmentmay be used so long as it can move separated insects (334) from onelocation to another. The separated insect conveyor (328) may route theseparated insects (334) to a downstream location such as to a grinder, apathogen removal unit, breeding chamber, a lipid extraction unit, or toa multifunctional flour mixing module.

In embodiments, the insect evacuation fan (312) is configured to removea portion of egg-laying insects from the insect feeding chamber byapplying a vacuum with a velocity pressure range from: between about0.001 inches of water to about 0.005 inches of water; between about0.005 inches of water to about 0.01 inches of water; between about 0.01inches of water to about 0.02 inches of water; between about 0.02 inchesof water to about 0.03 inches of water; between about 0.03 inches ofwater to about 0.04 inches of water; between about 0.04 inches of waterto about 0.05 inches of water; between about 0.05 inches of water toabout 0.06 inches of water; between about 0.06 inches of water to about0.07 inches of water; between about 0.07 inches of water to about 0.08inches of water; between about 0.08 inches of water to about 0.09 inchesof water; between about 0.09 inches of water to about 0.1 inches ofwater; between about 0.1 inches of water to about 0.2 inches of water;between about 0.2 inches of water to about 0.3 inches of water; betweenabout 0.3 inches of water to about 0.4 inches of water; between about0.4 inches of water to about 0.5 inches of water; between about 0.5inches of water to about 0.6 inches of water; between about 0.6 inchesof water to about 0.7 inches of water; between about 0.7 inches of waterto about 0.8 inches of water; between about 0.8 inches of water to about0.9 inches of water; between about 0.9 inches of water to about 1 inchof water; between about 1 inch of water to about 1.25 inches of water;between about 1.25 inches of water to about 1.5 inches of water; betweenabout 1.5 inches of water to about 2 inches of water; between about 2inches of water to about 3 inches of water; between about 3 inches ofwater to about 4 inches of water; between about 4 inches of water toabout 5 inches of water; between about 5 inches of water to about 6inches of water; between about 6 inches of water to about 7 inches ofwater; between about 7 inches of water to about 8 inches of water;between about 8 inches of water to about 9 inches of water; betweenabout 9 inches of water to about 10 inches of water; between about 10inch of water to about 15 inches of water; between about 15 inches ofwater to about 25 inches of water; between about 25 inches of water toabout 50 inches of water; between about 50 inches of water to about 75inches of water; between about 75 inches of water to about 100 inches ofwater; between about 100 inches of water to about 150 inches of water;between about 150 inches of water to about 200 inches of water; betweenabout 200 inches of water to about 250 inches of water; between about250 inches of water to about 300 inches of water; between about 300inches of water to about 350 inches of water; and, between about 350inches of water to about 400 inches of water.

FIG. 3 shows one non-limiting embodiment of an egg transfer system (244)including a conveyor (245) equipped with a first conveyor elevation unit(254) and a second conveyor elevation unit (256) that is configured toextend in a vertical direction from supports (255, 257) from a firstretracted height (H1) to a second elevated height (H2).

The conveyor (245) is configured to make an egg-depleted breedingmaterial (246) available to the interior (201) of the feeding chamber(200). This is achieved by providing a conveyor (245) having anegg-depleted breeding material (246) provided thereon and extending theconveyor (245) in a vertical direction so that the conveyor (245) andegg-depleted breeding material (246) come into contact with the screenfloor (258) of the feeding chamber (200). Egg-laying insects (225) laytheir eggs (259) through the screen floor (258) of the feeding chamber(200) and deposit the eggs (259) into the breeding material (248) thatrests upon the conveyor (245).

In the embodiment of FIG. 3, the egg-laying insects (225) present withinthe interior (201) of the feeding chamber (200) will deposit the eggs(259) into the breeding material (248) and the screen floor (258) willprevent them from eating or digging up the eggs (259). More on thedifferent states of operation is discussed below in FIGS. 5 through 10.

The conveyor (245) receives egg-depleted breeding material (246) via aconveyor input (247). The egg-depleted breeding material (246) is thenmade available to the insects (225) within the feeding chamber (200).This is made possible in the embodiment of FIG. 3 by activating thefirst conveyor elevation unit (254) and second conveyor elevation unit(256) so as to extend the conveyor (245) vertically in a directiontowards the bottom of the feeding chamber (200) from a first retractedheight (H1) to a second elevated height (H2).

After insects (225) have laid their eggs (259) into the breedingmaterial (248), the first conveyor elevation unit (254) and secondconveyor elevation unit (256) are returned from a first retracted height(H1) to a second elevated height (H2) so as to lower the conveyor (245)vertically in a direction away from the bottom of the feeding chamber(200).

As a result of eggs (259) being deposited into the egg-depleted breedingmaterial (246) an egg-laden breeding material (250) is created which isdischarged from the conveyor via a conveyor output (249). The egg-ladenbreeding material (250) has a greater amount of eggs within it inreference to the egg-depleted breeding material (246). The egg-ladenbreeding material (250) is then transferred to a breeding chamber asdescribed below in detail. The conveyor (245) is equipped with aconveyor motor (251) and a controller (252) that is configured to inputand output a signal (253) to the computer (COMP). The first conveyorelevation unit (254) has a first support (255) and the second conveyorelevation unit (256) has a second support (257). The breeding material(248) may be any conceivable material that is suitable for insects todeposit eggs into. In embodiments, the breeding material (248) is soil,mulch, compost, top soil, humus, clay, dirt, sand, minerals, organicmatter, or a combination thereof. In embodiments, the breeding material(248) may be comprised of a gel, a damp substrate, vermiculite, leaves,grass clippings, peat moss, agricultural residue, wood chips, greenwaste, woodchip mulch, bark chips, straw mulch, hay, food waste, animalwaste, cardboard, newspaper, carpet, foam, moss, recycled pulp, paperscraps, or feedstock, industrial waste, or any conceivable material thatis suitable for an insect to lay eggs in.

FIG. 3 also shows that the feeding chamber (200) has a hatched insectsinput (240) that is configured to transfer hatched insects (239) from abreeding chamber to the interior (201) of the feeding chamber (200) viaa breeding chamber insect transfer line (238). In embodiments where theInsect Production Superstructure System (IPSS) may have a plurality ofinsect feeding chambers (FC1, FC2, FC3), the first feeding chamber (FC1)is shown to have an egg-laying insects input (243) for transferringegg-laying insects (242) that were present within the second feedingchamber (FC2) or third feeding chamber (FC3) via a feeding chambertransfer line (241).

In embodiments, the feeding chamber grows insects within it over a timeduration ranging from: between about 1 week to 2 weeks; between about 2weeks to 3 weeks; between about 3 week to 4 weeks; between about 4 weekto 5 weeks; between about 5 week to 6 weeks; between about 6 week to 7weeks; between about 7 week to 8 weeks; between about 8 week to 9 weeks;between about 9 week to 10 weeks; between about 10 week to 11 weeks;between about 11 week to 12 weeks; between about 12 week to 13 weeks;between about 13 week to 14 weeks; or, between about 14 week to 15weeks.

FIG. 4

FIG. 4 shows one non-limiting embodiment of a network (220) of cells(219) for growing insects within a feeding chamber (200) of the insectfeeding module (2000) shown in FIG. 3.

FIG. 5

FIG. 5 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a second mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a second state at a second elevated height (H2) so as topermit insects (225) to lay eggs (259) within a provided breedingmaterial (248).

As discussed above in FIG. 3, FIG. 5 shows the conveyor (245) configuredto make breeding material (248) available to the interior (201) of thefeeding chamber (200). This is achieved by providing a conveyor (245)having a breeding material (248) provided thereon and extending theconveyor (245) in a vertical direction so that the conveyor (245) andegg-depleted breeding material (246) come into contact with the screenfloor (258) of the feeding chamber (200). Egg-laying insects (225) laytheir eggs (259) through the screen floor (258) of the feeding chamber(200) and deposit the eggs (259) into the breeding material (248) thatrests upon the conveyor (245).

In the embodiment of FIG. 5, the egg-laying insects (225) present withinthe interior (201) of the feeding chamber (200) will deposit the eggs(259) into the breeding material (248) and the screen floor (258) willprevent them from eating or digging up the eggs (259). The breedingmaterial (248) is made available to the insects (225) within the feedingchamber (200). This is made possible in the embodiment of FIG. 5 byactivating the first conveyor elevation unit (254) and second conveyorelevation unit (256) so as to extend the conveyor (245) vertically in adirection towards the bottom of the feeding chamber (200) from a firstretracted height (H1) to a second elevated height (H2).

As a result of eggs (259) being deposited into the egg-depleted breedingmaterial (246) an egg-laden breeding material (250) is created which isdischarged from the conveyor via a conveyor output (249). The egg-ladenbreeding material (250) has a greater amount of eggs within it inreference to the egg-depleted breeding material (246).

FIG. 6

FIG. 6 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a third mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a first state in a first retracted height (H1) so as todiscontinue insects (225) from laying eggs (259) within the providedbreeding material (248).

As a result of eggs (259) being deposited into the egg-depleted breedingmaterial (246) an egg-laden breeding material (250) is created which isdischarged from the conveyor via a conveyor output (249). The egg-ladenbreeding material (250) has a greater amount of eggs within it inreference to the egg-depleted breeding material (246).

FIG. 7

FIG. 7 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) and insect evacuation module (3000)operating in a fourth mode of operation wherein a vibration unit (214)is activated to permit the removal of insects (225) from the network(220) of cells (219) and wherein the insect evacuation module (3000)separates insects from gas while a vacuum is pulled on the insectfeeding module (2000) via an insect evacuation fan (312).

FIG. 8

FIG. 8 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein a plurality of slats (341) of an eggtransfer system (244) of the insect feeding module (2000) are in firstclosed state (341A).

Note that in FIG. 8, the enhanced feedstock input (206) is madeavailable to the feeding chamber (206) at a vertical height within theinterior below the network (220) of cells (219).

FIG. 8 discloses another embodiment of the feeding chamber (200) withouta screen floor (258). Instead, a plurality of slats (341) define thebottom of the feeding chamber (200). The plurality of slats (341) areequipped with a slat motor (344) and controller (345) configured torotate the slats (341) upon the input or output of a signal (346) to thecomputer (COMP). The slat motor (344) controller (345) is operativelyequipped to rotate the slats (341) into a plurality of states includinga first closed state (341A) and a second open state (341B). Theembodiments of FIGS. 8 and 9 show the plurality of rotatable slats (341)in the first closed state (341A).

The plurality of slats (341) define the lower section of the interior(201) of the feeding chamber (200) into an upper egg-laying section(342) and a lower egg transfer section (343). The upper egg-layingsection (342) is the region within the interior (201) of the feedingchamber above the plurality of slats (341) and below the network (220)of cells (219) where the insects reside. The lower egg transfer section(343) is the region below the plurality of slats (341) and above the eggtransfer system (244). The embodiment of FIG. 8 depicts the egg transfersystem (244) equipped to output an egg-laden breeding material (339) viaan egg-laden breeding material transfer line (340).

The embodiment of FIG. 8 also depicts the egg transfer system (244)equipped with egg-laden breeding material conveyor (347) with integralmass sensors (351, 353). Insects (225), as well as eggs (259), egg-ladenbreeding material (339) may also be removed via the egg transfer system(244). The egg-laden breeding material conveyor (347) has a motor (348)and a controller (349) that is configured to input and output a signal(350) to the computer (COMP). A first breeding material mass sensor(351) is operatively connected to the egg-laden breeding materialconveyor (347) and is configured to input a signal (352) to the computer(COMP). A second breeding material mass sensor (353) is operativelyconnected to the egg-laden breeding material conveyor (347) and isconfigured to input a signal (354) to the computer (COMP).

FIG. 9

FIG. 9 elaborates upon the non-limiting embodiment of FIG. 8 and showsbreeding material (248) resting upon the surface of the plurality ofslats (341) of the egg transfer system (244) so as to permit insects(225) to lay eggs (259) within the breeding material (248).

FIG. 10

FIG. 10 elaborates upon the non-limiting embodiment FIG. 8 but shows theegg transfer system (244) in a second open state (341A) so as to permitegg-laden breeding material (248) to pass through the plurality of slats(341) while the vibration unit (214) is activated, some insects (225)may pass through the open slats (341) as well.

FIG. 11

FIG. 11 shows a simplistic diagram illustrating an insect grindingmodule that is configured to grind at least a portion of the insectstransferred from the insect evacuation module (3000). A grinder (1250)is shown to grind the separated insects (334) into a stream of groundseparated insects (1500). The ground separated insects (1500) may besent to the lipid extraction unit (1501) on FIG. 12A, the pathogenremoval unit (1550) on FIG. 13, or the multifunctional flour mixingmodule (6000) on FIG. 14A.

FIG. 12A

FIG. 12A shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000).

FIG. 12A discloses a lipid extraction unit (1501) for extracting insectbased lipids in mass quantities for commercial scale output for use in avariety of areas throughout society. In embodiments, the lipidextraction unit (1501) includes a decanter (1502) having an interior(1505) defined by at least one side wall (1504). A weir (1503) may bepositioned in the decanter (1502). In embodiments, the lipid extractionunit (1501) may be a decanter (1502) in the form of a vertical orhorizontal decanter (1502). Separated insects (334) are provided to thelipid extraction unit (1501) from either the separated insect conveyor(328) via the separator or the ground separated insects (1500) via thegrinder (1250). Separated insects (334) are introduced to the lipidextraction unit (1501) via a separator insect input (1508) andoptionally introduced to the interior (1505) beneath the liquid level ofthe via a diptube (1509).

In embodiments, the lipid extraction unit (1501) is configured toextract lipids by use of a first immiscible liquid (1506) and a secondimmiscible liquid (1507). In embodiments, the first immiscible liquid(1506) has a first density (RHO1) and a first molecular weight (MW1),and the second immiscible liquid (1507) has a second density (RHO2), anda second molecular weight (MW2). In embodiments, first density (RHO1) isgreater than the second density (RHO2). In embodiments, first molecularweight (MW1) is greater than the second molecular weight (MW2).

In embodiments, the first immiscible liquid (1506) is an organiccompound, such as chloroform, with a first density (RHO1) of about 87pounds per cubic foot, and a first molecular weight (MW1) of about 119pound mass per pound mole. In embodiments, the second immiscible liquid(1507) is an alcohol, such as methanol, with a second density (RHO2) ofabout 44 pounds per cubic foot, and a second molecular weight (MW2) ofabout 32 pound mass per pound mole. In embodiments, the first density(RHO1) ranges from between about 70 pounds per cubic foot to about 110pounds per cubic foot. In embodiments, the second density (RHO2) rangesfrom between about 25 pounds per cubic foot to about 69 pounds per cubicfoot. In embodiments, the first molecular weight (MW1) ranges frombetween about 70 pound mass per pound mole to about 150 pound mass perpound mole. In embodiments, the second molecular weight (MW2) rangesfrom between about 18 pound mass per pound mole to about 69 pound massper pound mole.

The weir (1503) separates the decanter (1502) into a first section(1515) and a second section (1516). A first level sensor (1510) ispositioned within the interior (1505) to detect the level of theinterface region (1512) between the first immiscible liquid (1506) andthe second immiscible liquid (1507) within the first section (1515). Thefirst level sensor (1510) is configured to output a signal (1511) to thecomputer (COMP). A second level sensor (1513) is positioned within theinterior (1505) to detect the level of the second immiscible liquid(1507) within the second section (1516). The second level sensor (1513)is configured to output a signal (1514) to the computer (COMP).

In embodiments, a first immiscible liquid and lipid mixture (1518) isformed which is comprised of a lipid portion and a first immiscibleliquid portion. In embodiments, a second immiscible liquid andparticulate mixture (1521) is formed which is comprised of a particulateportion and a second immiscible liquid portion. In embodiments, theparticulate portion is comprised of one or more from the groupconsisting of insect legs, and wings, and protein. In embodiments, thesecond immiscible liquid (1507) floats above first immiscible liquid(1506) in the first section (1515) of the decanter (1502). An interfaceregion (1512) is the region in the first section (1515) of the decanter(1502) in between the upper second immiscible liquid (1507) and thelower first immiscible liquid (1506).

The decanter (1502) has a first immiscible liquid and lipid mixtureoutput (1517) for discharging a first immiscible liquid and lipidmixture (1518) towards a lipid transfer pump (1519). The decanter (1502)also has a second immiscible liquid and particulate mixture output(1520) for discharging a second immiscible liquid and particulatemixture (1521) towards a second immiscible liquid recirculation pump(1522) and particulate filter (1523). The particulate filter (1523) hasa second immiscible liquid input (1524), second immiscible liquid output(1525), and a filtered protein output (1532).

A particulate-depleted second immiscible liquid (1526) is dischargedfrom the second immiscible liquid output (1525) of the particulatefilter (1523) and returned to the decanter (1502) via aparticulate-depleted liquid input (1527). A filtered protein stream(1531) is discharged from the filtered protein output (1532) of theparticulate filter (1523). The decanter (1502) also has an interfacelayer protein take-off point (1528) configured to transfer an interfacelayer protein stream (1529) to an interface layer protein pump (1530).The interface layer protein stream (1529) is comprised of particulatesincluding insect legs, and wings, and protein from the interface region(1512). A temperature sensor (1533) is operatively connected to thelipid extraction unit (1501) and is configured to input a signal (1534)to the computer (COMP).

FIG. 12B

FIG. 12B shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000) byusing of no solvent by way of an expeller press.

FIG. 12B shows on non-limiting embodiment wherein lipids may be removedfrom insects without the use of a solvent. Specifically, the lipids maybe extracted from insects by use of a lipid extraction unit (1501) thatincorporates the use of a is a mechanical method for extracting oil. Forexample, one non-limiting embodiment shows the mechanical lipidextraction unit (1501) as an expeller press (1543).

The insects are squeezed through a pressing cage (1549) by the rotatingmotion of a screw press (1546) under high pressure. As the insects arepressed through the pressing cage (1549) by the screw press (1546),friction causes it to heat up. In embodiments, the temperature withinthe expeller press (1543) can increase due to the friction caused byextraction lipids (1541) from the insects. This requires the expellerpress (1543) to require a source of cooling water to cool regulatetemperature and prevent overheating. Ground separated insects (1500)from the separated insect conveyor (328) or insects from any variety offeeding chambers (FC2, FC2, FC3) may be transferred to the lipidextraction unit (1501) by way of a conveyor (1535). The conveyor (1535)transfers lipid laden insects (1537) to the mechanical lipid extractionunit (1501).

The mechanical lipid extraction unit (1501) extracts lipids (1541) fromthe lipid laden insects (1537) to form a stream of lipid depletedinsects (1538). In embodiments, the lipid depleted insects (1538) arecomprised of protein (1542). The conveyor (1535) is equipped with a flowsensor (1536A) that is configured to input/output a signal (1536B) tothe computer (COMP). The conveyor (1535) transfers lipid laden insects(1537) to the feed bin (1544) of the expeller press (1543).

The expeller press (1543) includes a feed bin (1544), motor (1545), andhaving an interior containing a screw press (1546). The screw press(1546) is equipped with a shaft (1547) and flights (1548) and isconfigured to extract lipids from insects by applying pressure on theinsects to squeeze liquid lipids (1541) from the insects. Liquid lipids(1541) extracted from the insects is discharged from the expeller press(1543) through a pressing cage (1549) and a lipid output (1551) and alipid transfer line (1552). A lipid composition sensor (1539) isinstalled on the lipid transfer line (1552) and is configured to inputor output a signal (1540) to the computer (COMP). The expeller press(1543) is equipped with a stand (1555) to elevate off of the ground. Theexpeller press (1543) is equipped with a protein output (1553). Theprotein output (1553) may be an annular nozzle (1554). Lipid depletedinsects (1538) are discharged from the expeller press (1543) via theprotein output (1553). In embodiments, the lipid depleted insects (1538)contain protein (1542). The lipids (1541) may in embodiments be anemulsion. In embodiment, the lipids (1541) emulsion may be an emulsionof oil and water.

The lipid depleted insects (1538) are comprised of a reduced amount oflipids (1541) relative to the lipid laden insects (1537). Lipid depletedinsects (1538) exiting the protein output (1553) are routed to a proteinconveyor (1556). The protein conveyor (1556) is equipped with a pathogensensor (1557) that is configured to input or output a signal (1558) tothe computer (COMP). A protein transfer conduit (1559) is connected tothe protein conveyor (1556) and is configured to remove lipid depletedinsects (1538) containing protein (1542). The mechanical lipidextraction unit (1501) is equipped with a cooling water input (1561) anda cooling water output (1562). A cooling water input temperature sensor(1563) configured to input and output a signal (1564) to the computer(COMP) is installed on the cooling water input (1561). A cooling wateroutput temperature sensor (1566) configured to input and output a signal(1567) to the computer (COMP) is installed on the cooling water output(1562).

In embodiments, the cooling water input temperature sensor (1563) readsa temperature ranging from between about 60 degrees Fahrenheit to about150 degrees Fahrenheit. In embodiments, the cooling water outputtemperature sensor (1566) reads a temperature ranging from between about150.999 degrees Fahrenheit to about 210 degrees Fahrenheit. Inembodiments, the expeller temperature sensor (1568) reads a temperatureranging from between about 60 degrees Fahrenheit to about 210 degreesFahrenheit.

In embodiments, the lipid extraction unit (1501) is equipped with anexpeller pressure sensor (1571) that is configured to input or output asignal to the computer (COMP). In embodiments, the expeller pressuresensor (1571) reads a pressure within the expeller press (1543) rangesfrom: between about 0.25 PSI to about 49.99 PSI; between about 50 PSI toabout 99.99 PSI; between about 100 PSI to about 149.99 PSI; betweenabout 150 PSI to about 199.99 PSI; between about 200 PSI to about 249.99PSI; between about 250 PSI to about 299.99 PSI; between about 300 PSI toabout 349.99 PSI; between about 350 PSI to about 399.99 PSI; betweenabout 400 PSI to about 449.99 PSI; between about 450 PSI to about 499.99PSI; between about 500 PSI to about 549.99 PSI; between about 550 PSI toabout 599.99 PSI; between about 600 PSI to about 649.99 PSI; betweenabout 650 PSI to about 699.99 PSI; between about 700 PSI to about 749.99PSI; between about 750 PSI to about 799.99 PSI; between about 800 PSI toabout 8549.99 PSI; between about 850 PSI to about 899.99 PSI; betweenabout 900 PSI to about 949.99 PSI; between about 950 PSI to about 999.99PSI; between about 1,000 PSI to about 1,499.99 PSI; between about 1,500PSI to about 1,999.99 PSI; between about 2,000 PSI to about 2,499.99PSI; between about 2,500 PSI to about 2,999.99 PSI; between about 3,000PSI to about 3,499.99 PSI; between about 3,500 PSI to about 3,999.99PSI; between about 4,000 PSI to about 4,499.99 PSI; between about 4,500PSI to about 4,999.99 PSI; between about 5,000 PSI to about 5,499.99PSI; between about 5,500 PSI to about 5,999.99 PSI; between about 6,000PSI to about 6,499.99 PSI; between about 6,500 PSI to about 6,999.99PSI; between about 7,000 PSI to about 7,499.99 PSI; between about 7,500PSI to about 7,999.99 PSI; between about 8,000 PSI to about 8,499.99PSI; between about 8,500 PSI to about 8,999.99 PSI; between about 9,000PSI to about 9,499.99 PSI; between about 9,500 PSI to about 9,999.99PSI; between about 10,000 PSI to about 15,499.99 PSI; between about15,500 PSI to about 19,999.99 PSI; between about 20,000 PSI to about25,499.99 PSI; between about 25,500 PSI to about 29,999.99 PSI; betweenabout 30,000 PSI to about 35,499.99 PSI; and, between about 35,500 PSIto about 40,000 PSI.

It has been my realization that in one non-limiting embodiment the bestmode to operate one scale of an expeller press (1543) is so that theexpeller pressure sensor (1571) reads a pressure of about 250 PSI. Ithas been my realization that in one non-limiting embodiment the bestmode to operate one scale of an expeller press (1543) is so that theexpeller pressure sensor (1571) reads a pressure of about 4,900 PSI. Ithas been my realization that in one non-limiting embodiment the bestmode to operate one scale of an expeller press (1543) is so that theexpeller pressure sensor (1571) reads a pressure of about 19,900 PSI.Nonetheless, all of the above pressures may work as intended to realizelipid extraction from insects.

FIG. 13

FIG. 13 shows a simplistic diagram illustrating a pathogen removalmodule that is configured to remove pathogens from at least a portion ofthe insects transferred from the insect evacuation module (3000). Insome embodiments, a water bath (1581) containing hot water (1582) may beused to remove pathogens from the insects. In embodiments, thetemperature of the water bath (1581) includes a water bath temperaturesensor (1583) that is configured to input or output a signal (1584) tothe computer. In embodiment, the water bath temperature sensor (1583)indicates that the water bath (1581) operates at a temperature rangingfrom between: about 120 degrees Fahrenheit to about 130 degreesFahrenheit; about 130 degrees Fahrenheit to about 140 degreesFahrenheit; about 140 degrees Fahrenheit to about 150 degreesFahrenheit; about 150 degrees Fahrenheit to about 160 degreesFahrenheit; about 160 degrees Fahrenheit to about 170 degreesFahrenheit; about 170 degrees Fahrenheit to about 180 degreesFahrenheit; about 180 degrees Fahrenheit to about 190 degreesFahrenheit; about 190 degrees Fahrenheit to about 200 degreesFahrenheit; and, about 200 degrees Fahrenheit to about 212 degreesFahrenheit.

FIG. 14A

FIG. 14A shows a simplistic diagram illustrating a multifunctional flourmixing module that is configured to generate a multifunctional flourfrom at least a portion of the insects transferred from the pathogenremoval module and including the sequence steps or sub-modules includingan insect distribution module (6A), fiber-starch distribution module(6B), binding agent distribution module (6C), density improving texturalsupplement distribution module (6D), moisture improving texturalsupplement distribution module (6E), multifunctional flour mixing module(6F).

Insect Distribution Module (6A)

FIG. 14A displays an insect distribution module (6A) including an insecttank (6A2) that is configured to accept insects (6A1). The insect tank(6A2) has an interior (6A3), an insect input (6A4), an insect conveyor(6A5), and an insect conveyor output (6A6). The insect tank (6A2)accepts insects (6A1) to the interior (6A3) and regulates and controlsan engineered amount of insects (6A1) downstream to be mixed to form amultifunctional flour. The insect conveyor (6A5) has an integratedinsect mass sensor (6A7) that is configured to input and output a signal(6A8) to the computer (COMP). The insect conveyor motor (6A9) has acontroller (6A10) that is configured to input and output a signal (6A11)to the computer (COMP). The insect mass sensor (6A7), insect conveyor(6A5), and insect conveyor motor (6A9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of insect (6A1)via an insect transfer line (6A12).

Fiber-Starch Distribution Module (6B)

FIG. 14A displays a fiber-starch distribution module (6B) including afiber-starch tank (6B2) that is configured to accept fiber-starch (6B1).The fiber-starch tank (6B2) has an interior (6B3), a fiber-starch input(6B4), a fiber-starch conveyor (6B5), and a fiber-starch conveyor output(6B6). The fiber-starch tank (6B2) accepts fiber-starch (6B1) to theinterior (6B3) and regulates and controls an engineered amount offiber-starch (6B1) downstream to be mixed to form a multifunctionalflour. The fiber-starch conveyor (6B5) has an integrated fiber-starchmass sensor (6B7) that is configured to input and output a signal (6B8)to the computer (COMP). The fiber-starch conveyor motor (6B9) has acontroller (6B10) that is configured to input and output a signal (6B11)to the computer (COMP). The fiber-starch mass sensor (6B7), fiber-starchconveyor (6B5), and fiber-starch conveyor motor (6B9) are coupled so asto permit the conveyance, distribution, or output of a precise flow offiber-starch (6B1) via a fiber-starch transfer line (6B12).

Binding Agent Distribution Module (6C)

FIG. 14A displays a binding agent distribution module (6C) including abinding agent tank (6C2) that is configured to accept a binding agent(6C1). The binding agent tank (6C2) has an interior (6C3), a bindingagent input (6C4), a binding agent conveyor (6C5), and a binding agentconveyor output (6C6). The binding agent tank (6C2) accepts bindingagent (6C1) to the interior (6C3) and regulates and controls anengineered amount of a binding agent (6C1) downstream to be mixed toform a multifunctional flour. The binding agent conveyor (6C5) has anintegrated binding agent mass sensor (6C7) that is configured to inputand output a signal (6C8) to the computer (COMP). The binding agentconveyor motor (6C9) has a controller (6C10) that is configured to inputand output a signal (6C11) to the computer (COMP). The binding agentmass sensor (6C7), binding agent conveyor (6C5), and binding agentconveyor motor (6C9) are coupled so as to permit the conveyance,distribution, or output of a precise flow of binding agent (6C1) via abinding agent transfer line (6C12).

Density Improving Textural Supplement Distribution Module (6D)

FIG. 14A displays a density improving textural supplement distributionmodule (6D) including a density improving textural supplement tank (6D2)that is configured to accept a density improving textural supplement(6D1). The density improving textural supplement tank (6D2) has aninterior (6D3), a density improving textural supplement input (6D4), adensity improving textural supplement conveyor (6D5), and a densityimproving textural supplement conveyor output (6D6). The densityimproving textural supplement tank (6D2) accepts density improvingtextural supplement (6D1) to the interior (6D3) and regulates andcontrols an engineered amount of a density improving textural supplement(6D1) downstream to be mixed to form a multifunctional flour. Thedensity improving textural supplement conveyor (6D5) has an integrateddensity improving textural supplement mass sensor (6D7) that isconfigured to input and output a signal (6D8) to the computer (COMP).The density improving textural supplement conveyor motor (6D9) has acontroller (6D10) that is configured to input and output a signal (6D11)to the computer (COMP). The density improving textural supplement masssensor (6D7), density improving textural supplement conveyor (6D5), anddensity improving textural supplement conveyor motor (6D9) are coupledso as to permit the conveyance, distribution, or output of a preciseflow of density improving textural supplement (6D1) via a densityimproving textural supplement transfer line (6D12).

Moisture Improving Textural Supplement Distribution Module (6E)

FIG. 14A displays a moisture improving textural supplement distributionmodule (6E) including a moisture improving textural supplement tank(6E2) that is configured to accept a moisture improving texturalsupplement (6E1). The moisture improving textural supplement tank (6E2)has an interior (6E3), a moisture improving textural supplement input(6E4), a moisture improving textural supplement conveyor (6E5), and amoisture improving textural supplement conveyor output (6E6). Themoisture improving textural supplement tank (6E2) accepts a moistureimproving textural supplement (6E1) to the interior (6E3) and regulatesand controls an engineered amount of a moisture improving texturalsupplement (6E1) downstream to be mixed to form a multifunctional flour.The moisture improving textural supplement conveyor (6E5) has anintegrated moisture improving textural supplement mass sensor (6E7) thatis configured to input and output a signal (6E8) to the computer (COMP).The moisture improving textural supplement conveyor motor (6E9) has acontroller (6E10) that is configured to input and output a signal (6E11)to the computer (COMP). The moisture improving textural supplement masssensor (6E7), moisture improving textural supplement conveyor (6E5), andmoisture improving textural supplement conveyor motor (6E9) are coupledso as to permit the conveyance, distribution, or output of a preciseflow of moisture improving textural supplement (6E1) via a moistureimproving textural supplement transfer line (6E12).

Cannabis Enhancer Distribution Module (6 g)

FIG. 14A displays a cannabis enhancer distribution module (6G) includinga cannabis enhancer tank (6G2) that is configured to accept a cannabisenhancer (6G1). The cannabis enhancer tank (6G2) has an interior (6G3),a cannabis enhancer input (6G4), a cannabis enhancer conveyor (6G5), anda cannabis enhancer conveyor output (6G6). The cannabis enhancer tank(6G2) accepts a cannabis enhancer (6G1) to the interior (6G3) andregulates and controls an engineered amount of a cannabis enhancer (6G1)downstream to be mixed to form a multifunctional flour. The cannabisenhancer conveyor (6G5) has an integrated cannabis enhancer mass sensor(6G7) that is configured to input and output a signal (6G8) to thecomputer (COMP). The cannabis enhancer conveyor motor (6G9) has acontroller (6G10) that is configured to input and output a signal (6G11)to the computer (COMP). The cannabis enhancer mass sensor (6G7),cannabis enhancer conveyor (6G5), and cannabis enhancer conveyor motor(6G9) are coupled so as to permit the conveyance, distribution, oroutput of a precise flow of cannabis enhancer (6G1) via a cannabisenhancer transfer line (6G12).

Multifunctional Flour Mixing Module (6F)

FIG. 14A displays a multifunctional flour mixing module (6F) including amultifunctional flour tank (6F1) that is configured to accept a mixtureincluding insects (6A1), fiber-starch (6B1), binding agent (6C1),density improving textural supplement (6D1), moisture improving texturalsupplement (6E1), and cannabis enhancer (6G1) via a multifunctionalflour transfer line (6F0). The insects (6A1) may be pathogen-depletedinsects (1570) transferred from the pathogen removal unit (1550) asdepicted in FIG. 14A. FIG. 14B shows the insects (6A1) as groundseparated insects (1500) transferred from the grinder (1250). Themultifunctional flour tank (6F1) has an interior (6F2), amultifunctional flour tank input (6F3), screw conveyor (6F9),multifunctional flour output (6F10). The multifunctional flour tank(6F1) accepts insects (6A1), fiber-starch (6B1), binding agent (6C1),density improving textural supplement (6D1), moisture improving texturalsupplement (6E1), and cannabis enhancer (6G1) to the interior (6F2) andmixes, regulates, and outputs a weighed multifunctional flour stream(6F22).

The multifunctional flour tank (6F1) has a top section (6F4), bottomsection (6F5), at least one side wall (6F6), with a level sensor (6F7)positioned thereon that is configured to input and output a signal (6F8)to the computer (COMP). The screw conveyor (6F9) has a multifunctionalflour conveyor motor (6F11) with a controller (6F12) that is configuredto input and output a signal (6F13) to the computer (COMP). From themultifunctional flour output (6F10) of the multifunctional flour tank(6F1) is positioned a multifunctional flour weigh screw (6F14) that isequipped with a multifunctional flour weigh screw input (6F15), amultifunctional flour weigh screw output (6F16), and a mass sensor(6F17) that is configured to input and output a signal (6F18) to thecomputer (COMP). The multifunctional flour weigh screw (6F14) also has aweigh screw motor (6F19) with a controller (6F20) that is configured toinput and output a signal (6F21) to the computer (COMP).

FIG. 14B

FIG. 14B shows a simplistic diagram illustrating a multifunctional flourmixing module that is configured to generate a multifunctional flour asdescribed in FIG. 14A however instead from at least a portion of theinsects transferred from the insect grinding module.

FIG. 14C

FIG. 14C shows one non-limiting embodiment of a liquid mixing module(LMM) that is configured to mix water with multifunctional flour (6F23)provided from the multifunctional flour mixing module as shown in FIG.14A or 14B.

FIG. 14C shows one non-limiting embodiment of a liquid mixing module(LMM) that includes a first water treatment unit (C10), a second watertreatment unit (C11), and a third water treatment unit (C12), thatprovide a third contaminant depleted water (C13) to the interior (C14)of a mixing tank (C15). The mixing tank (C15) mixes a water supply (C16)with multifunctional flour (6F23) provided from the multifunctionalflour mixing module as shown in FIG. 14A or 14B to form amultifunctional flour and water mixture (C17). The multifunctional flour(6F23) introduced to the mixing tank (C15) may be a weighedmultifunctional flour stream (6F22).

The multifunctional flour and water mixture (C17) is transferred fromthe mixing tank (C15) to the shaping module (14D) of FIG. 14D. Inembodiments, the multifunctional flour and water mixture (C17) istransferred and pressurized using a pump (C18) from the mixing tank(C15) to the shaping module (14D) of FIG. 14D. In embodiments, themultifunctional flour and water mixture (C17) is transferred andpressurized using a screw auger (C19) from the mixing tank (C15) to theshaping module (14D) of FIG. 14D.

FIG. 14C depicts the first water treatment unit (C10) to include acation, a second water treatment unit (C11) to include an anion, and athird water treatment unit (C13) to include a membrane. A first waterpressure sensor (C20) is positioned on the water input conduit (C21)that is introduced to the first input (C22) to the first water treatmentunit (C10). In embodiments, a filter (C23), activated carbon (C24),and/or an adsorbent (C25), are positioned on the water input conduit(C21) prior to introducing the water supply (C16) to the first watertreatment unit (C10).

The water supply (C16) may be considered a contaminant-laden water (C26)that includes positively charged ions, negatively charged ions, andundesirable compounds. The positively charged ions are comprised of oneor more from the group consisting of calcium, magnesium, sodium, andiron. The negatively charged ions are comprised of one or more from thegroup consisting of iodine, chloride, and sulfate. The undesirablecompounds are comprised of one or more from the group consisting ofdissolved organic chemicals, viruses, bacteria, and particulates.

A first contaminant depleted water (C27) is discharged by the firstwater treatment unit (C10) by a first output (C28). The firstcontaminant depleted water (C27) may be a positively charged iondepleted water (C29). The first contaminant depleted water (C27) is thentransferred to the second water treatment unit (C11) via a second input(C30). A second contaminant depleted water (C31) is discharged by thesecond water treatment unit (C11) by a second output (C32). The secondcontaminant depleted water (C31) may be a negatively charged iondepleted water (C33). The second contaminant depleted water (C31) isthen transferred to the third water treatment unit (C12) via a thirdinput (C34). A third contaminant depleted water (C13) is discharged bythe third water treatment unit (C12) by a third output (C35). The thirdcontaminant depleted water (C13) may be an undesirable compoundsdepleted water (C36). The third contaminant depleted water (C13) is thentransferred to the interior (C14) of a mixing tank (C15) via a watersupply conduit (C37) and water input (C38).

Within the interior (C14) of a mixing tank (C15), the water is mixedwith multifunctional flour (6F23) provided from the multifunctionalflour mixing module as shown in FIG. 14A or 14B. In embodiments, acation (C39), an anion (C40), and a polishing unit (C41), are positionedon the water supply conduit (C37) in between the third water treatmentunit (C12) and the water input (C38) of the mixing tank (C15). Thepolishing unit (C41) may be any type of conceivable device to improvethe water quality such as an ultraviolet unit, ozone unit, microwaveunit, filter, or the like.

In embodiments, water supply valve (C42) is positioned on the watersupply conduit (C37) in between the third water treatment unit (C12) andthe water input (C38) of the mixing tank (C15). The water supply valve(C42) is equipped with a controller (C43) that inputs or outputs asignal from a computer (COMP). In embodiments, the mixing tank (C15) isequipped with a high-level sensor (C44) and a low-level sensor (C45).The high-level sensor (C44) is used for detecting a high level and thelow-level sensor (C45) is used for detecting a low level. The high-levelsensor (C44) is configured to output a signal to the computer (COMP)when the high-level sensor (C44) is triggered by a high level of liquidwithin the mixing tank (C15). The low-level sensor (C45) is configuredto output a signal to the computer (COMP) when the low-level sensor(C45) is triggered by a low level of liquid within the mixing tank(C15).

In embodiments, when the low-level sensor (C45) sends a signal to thecomputer (COMP), the water supply valve (C42) on the water supplyconduit (C37) is opened and introduces water into the mixing tank (C15)until the high-level sensor (C44) is triggered thus sending a signal tothe computer (COMP) to close the water supply valve (C42). This levelcontrol loop including the high-level sensor (C44) for detecting a highlevel and a low-level sensor (C45) for detecting a lower level may becoupled to the operation of the water supply valve (C42) for introducinga water supply (C16) through a first water treatment unit (C10), asecond water treatment unit (C11), and a third water treatment unit(C12), to provide a third contaminant depleted water (C13) to theinterior (C14) of a mixing tank (C15).

The mixing tank (C15) may be placed on a load cell (C46) for measuringthe mass of the tank. The mixing tank (C15) may be equipped with a mixer(C47) for mixing water with multifunctional flour (6F23). Themultifunctional flour (6F23) is introduced to the interior (C14) of themixing tank (C15) via an input (C51). The mixer (C47) may be of an augeror blade type that is equipped with a motor (C48). The mixing tank (C15)has a multifunctional flour and water mixture output (C49) that isconnected to a discharge conduit (C50).

The discharge conduit (C50) is connected at one end to themultifunctional flour and water mixture output (C49) of the mixing tank(C15) and at another end to a supply pump (C18) or a screw auger (C19).The supply pump (C18) or a screw auger (C19) provides a pressurizedsource of multifunctional flour and water mixture (C17) to thedownstream shaping module (14D) as shown in FIG. 14D. Themultifunctional flour and water mixture (C17) may be a pressurizedmultifunctional flour and water mixture (C17A).

In embodiments, a flow sensor (C51) and/or a flow totalizer (C52) may beinstalled on the water supply conduit (C37) to determine the mass orvolume of water that is sent to the interior (C14) of the mixing tank(C15). In embodiments, the mixing tank (C15) is equipped with a heatexchanger (C53) to heat the mixture of water and multifunctional flour.The heat exchanger (C53) may be electrically heated or provided with asource of steam or hot oil.

In embodiments, the mass of water or multifunctional flour within themixing tank (C15) can be measured via the load cell (C46). Inembodiments, water can be added to the mixing tank (C15) and the mass ofwater is measured, following by adding the multifunctional flour to theinterior (C14) of the mixing tank (C15) to know the mass of the totalmixture. The contents within the mixing tank (C15) can be mixed with themixer and optionally heated.

FIG. 14D

FIG. 14D shows one non-limiting embodiment of a shaping module (14D)that is configured to shape the multifunctional flour and water mixture(C17) to produce a shaped multifunctional flour mixture (D10).

Many shaping technologies are available to shape the multifunctionalflour and water mixture (C17) including one or more from the groupconsisting of extrusion, sheeting rolling, and cutting rolls. Extrusionis a process used to create a shaped multifunctional flour mixture (D10)having a fixed cross-sectional profile. The die (D15) has a fixedcross-sectional profile and is configured to accept the multifunctionalflour and water mixture (C17) and press it into an extrudate (D11). Themultifunctional flour and water mixture (C17) is pushed through a die ofthe desired cross-section to create an extrudate (D11) or a shapedmultifunctional flour mixture (D10) which may then be cooked in acooking module (14E) as shown in FIG. 14E.

In embodiments, the shaping module (14D) includes an extrusion system(D12). In embodiments, the extrusion system (D12) includes an inputhopper (D13), an auger (D14), and a die (D15). The auger (D14) is drivenby a motor (D16). The multifunctional flour and water mixture (C17) istransferred from the liquid mixing module (LMM) as shown in FIG. 14C andprovided to the input hopper (D13) of the extrusion system (D12).

The multifunctional flour and water mixture (C17) is transferred throughthe die (D15) by the rotating motion of an auger (D14). As themultifunctional flour and water mixture (C17) is pressed through the die(D15) by the auger (D14), friction causes at least a portion of theextrusion system (D12) to generate heat. In embodiments, the temperaturewithin the extrusion system (D12) can increase due to the frictioncaused by formation of the extrudate (D11). This requires the extrusionsystem (D12) to require a source of coolant, such as cooling water, tocool regulate temperature and prevent overheating. In embodiments, theauger (D14) is cooled with a coolant. The auger (D14) is equipped with ashaft (D17) and flights (D18) and is configured to applying pressure onthe multifunctional flour and water mixture (C17) sufficient to squeezethrough the die (D15). The shaped multifunctional flour mixture (D10) oran extrudate (D11) is discharged from the extrusion system (D12) via aextrudate output (D19). The extrusion system (D12) is equipped with astand (D20) to elevate it off the ground.

The shaped multifunctional flour mixture (D10) or an extrudate (D11) isdischarged from the extrusion system (D12) via a extrudate output (D19)and is transferred to a conveyor (D21). The conveyor (D21) transfers theextrudate (D11) to the cooking module (14E) as shown in FIG. 14E. Theconveyor (D21) may be mechanical, pneumatic, air conveyor, elevatingconveyor, conveyor belt, a drag-chain conveyor, bucket elevator, or anyconceivable means to transfer extrudate (D11) from the extrusion system(D12) to the cooking module (14E).

In embodiments, the extrusion system (D12) is equipped with an extrusionpressure sensor (D21) that is configured to input or output a signal(D22) to the computer (COMP). In embodiments, the extrusion pressuresensor (D21) reads a pressure within the extrusion system (D12) rangingfrom: between about 0.25 PSI to about 49.99 PSI; between about 50 PSI toabout 99.99 PSI; between about 100 PSI to about 149.99 PSI; betweenabout 150 PSI to about 199.99 PSI; between about 200 PSI to about 249.99PSI; between about 250 PSI to about 299.99 PSI; between about 300 PSI toabout 349.99 PSI; between about 350 PSI to about 399.99 PSI; betweenabout 400 PSI to about 449.99 PSI; between about 450 PSI to about 499.99PSI; between about 500 PSI to about 549.99 PSI; between about 550 PSI toabout 599.99 PSI; between about 600 PSI to about 649.99 PSI; betweenabout 650 PSI to about 699.99 PSI; between about 700 PSI to about 749.99PSI; between about 750 PSI to about 799.99 PSI; between about 800 PSI toabout 8549.99 PSI; between about 850 PSI to about 899.99 PSI; betweenabout 900 PSI to about 949.99 PSI; between about 950 PSI to about 999.99PSI; between about 1,000 PSI to about 1,499.99 PSI; between about 1,500PSI to about 1,999.99 PSI; between about 2,000 PSI to about 2,499.99PSI; between about 2,500 PSI to about 2,999.99 PSI; between about 3,000PSI to about 3,499.99 PSI; between about 3,500 PSI to about 3,999.99PSI; between about 4,000 PSI to about 4,499.99 PSI; between about 4,500PSI to about 4,999.99 PSI; between about 5,000 PSI to about 5,499.99PSI; between about 5,500 PSI to about 5,999.99 PSI; between about 6,000PSI to about 6,499.99 PSI; between about 6,500 PSI to about 6,999.99PSI; between about 7,000 PSI to about 7,499.99 PSI; between about 7,500PSI to about 7,999.99 PSI; between about 8,000 PSI to about 8,499.99PSI; between about 8,500 PSI to about 8,999.99 PSI; between about 9,000PSI to about 9,499.99 PSI; between about 9,500 PSI to about 9,999.99PSI; between about 10,000 PSI to about 15,499.99 PSI; between about15,500 PSI to about 19,999.99 PSI; between about 20,000 PSI to about25,499.99 PSI; between about 25,500 PSI to about 29,999.99 PSI; betweenabout 30,000 PSI to about 35,499.99 PSI; and, between about 35,500 PSIto about 40,000 PSI.

It has been my realization that in one non-limiting embodiment the bestmode to operate the extrusion system (D12) includes maintaining theextrusion pressure sensor (D21) at a pressure less than 250 PSI.Nonetheless, all the above pressures may work as intended to realize ashaped multifunctional flour mixture (D10).

The extrusion system (D12) may be equipped with a coolant input (D23)and a coolant output (D24). A coolant input temperature sensor (D25) isconfigured to input and output a signal (D26) to the computer (COMP) andmeasures the temperature of coolant that passes into the coolant input(D23). A coolant output temperature sensor (D27) is configured to inputand output a signal (D28) to the computer (COMP) and measures thetemperature of coolant that leaves the coolant output (D24). A coolant(D29) passes from the coolant input (D23) to the coolant output (D24)and accepts heat from at least a portion of the extrusion system (D12).The temperature of the coolant (D29) measured at the coolant outputtemperature sensor (D27) is greater than the temperature measured by thecoolant input temperature sensor (D25).

In embodiments, the coolant input temperature sensor (D25) reads atemperature ranging from between about 60 degrees Fahrenheit to about150 degrees Fahrenheit. In embodiments, the coolant output temperaturesensor (D27) reads a temperature ranging from between about 150.999degrees Fahrenheit to about 210 degrees Fahrenheit.

FIG. 14E

FIG. 14E shows one non-limiting embodiment of a cooking module (14E)that is configured to cook the shaped multifunctional flour mixture(D10) provided from the shaping module (14D) to form a cookedmultifunctional flour mixture (E18A).

FIG. 14E shows one non-limiting embodiment of a cooking module (14E)that is configured to cook the shaped multifunctional flour mixture(D10) or extrudate (D11) provided from the shaping module (14D) to forma cooked multifunctional flour mixture (E18A).

The cooking module (14E) as shown in FIG. 14E includes a cooking system(E10). The cooking system (E10) shown in FIG. 14D includes an oven (E11)or a fryer (E12). In embodiments, the fryer (E12) cooks the extrudate(D11) in an oil (E19). In embodiments, the oil (E19) are lipidsextracted from insects as shown in FIGS. 12A and/or 12B. In embodiments,the oil (E19) may be comprised of one or more from the group consistingof almond oil, animal-based oils, apricot kernel oil, avocado oil,brazil nut oil, butter, canola oil, cashew oil, cocoa butter, coconutoil, cooking oil, corn oil, cottonseed oil, fish oil, grapeseed oil,hazelnut oil, hemp oil, insect oil, lard, lard oil, macadamia nut oil,mustard oil, olive oil, palm kernel oil, palm oil, peanut oil, rapeseedoil, rice oil, rice bran oil, safflower oil, semi-refined sesame oil,semi-refined sunflower oil, sesame oil, soybean oil, tallow of beef,tallow of mutton, vegetable oil, and walnut oil. The cooking system(E10) may also include a dryer (E13), pressure cooker (E14), dehydrator(E15), freeze dryer (E16), and may operate in a batch or continuousmode.

A conveyor (E17) may be integrated with the cooking system (E10). Theconveyor (E17) may be mechanical, pneumatic, air operated, an elevatingconveyor, conveyor belt, drag-chain conveyor, or the like.

The cooking system (E10) cooks the extrudate (D11) provided from theshaping module (14D) to form a cooked extrudate (E18) or a cookedmultifunctional flour mixture (E18A). The cooked extrudate (E18) orcooked multifunctional flour mixture (E18A) is transferred to theflavoring module (14F) as shown in FIG. 14F. In embodiments, the cookedmultifunctional flour mixture (E18A) is a cooked extrudate (E18).

In embodiments, the cooking system (E10) cooks the extrudate (D11) at atemperature ranging from between: 100 degrees F. to 124.99 degrees F.;125 degrees F. to 149.99 degrees F.; 150 degrees F. to 174.99 degreesF.; 175 degrees F. to 199.99 degrees F.; 200 degrees F. to 224.99degrees F.; 225 degrees F. to 249.99 degrees F.; 250 degrees F. to274.99 degrees F.; 275 degrees F. to 299.99 degrees F.; 300 degrees F.to 324.99 degrees F.; 325 degrees F. to 349.99 degrees F.; 350 degreesF. to 374.99 degrees F.; 375 degrees F. to 399.99 degrees F.; 400degrees F. to 550 degrees F.

In embodiments, the cooking system (E10) cooks the extrudate (D11) overa time duration ranging from between: 1 second to 5 seconds, 5 secondsto 15 seconds; 15 seconds to 30 seconds; 30 seconds to 1 minute; 1minute to 2 minutes; 2 minutes to 3 minutes; 3 minutes to 4 minutes; 4minutes to 5 minutes; 5 minutes to 6 minutes; 6 minutes to 7 minutes; 7minutes to 8 minutes; 8 minutes to 9 minutes; 9 minutes to 10 minutes;11 minutes to 12 minutes; 12 minutes to 13 minutes; 13 minutes to 14minutes; 14 minutes to 15 minutes; 15 minutes to 16 minutes; 16 minutesto 17 minutes; 17 minutes to 18 minutes; 18 minutes to 19 minutes; 19minutes to 60 minutes.

FIG. 14F

FIG. 14F shows one non-limiting embodiment of a flavoring module (14F)that is configured to flavor the cooked multifunctional flour mixture(E18A) provided from the cooking module (14E) to form a flavoredmultifunctional flour mixture (F10).

FIG. 14F shows one non-limiting embodiment of a flavoring module (14F)that is configured to flavor the cooked extrudate (E18) provided fromthe cooking module (14E) to form a flavored cooked extrudate (F10).

The flavoring module (14F) as shown in FIG. 14F includes a flavoringsystem (F11). The flavoring system (F11) shown in FIG. 14F includes aflavoring machine (F12) shown in the form of a tumbler (F13). Thetumbler (F13) has a motor (F14) and a controller (F15) and is configuredto be operated by a computer (COMP). The flavoring machine (F12) has acooked extrudate input (F16) for receiving the cooked extrudate (E18)from the cooking module (14E).

The flavoring machine (F12) has a flavoring input (F17) for receivingflavoring (F18). The flavoring (F18) are comprised of one or more fromthe group consisting of allspice berries, almond meal, anise seed,annato seed, arrowroot powder, basil, bay leaves, black pepper,buttermilk, cannabis, caraway, cayenne, celery seed, cheese cultures,chervil, Chile powder, chives, cilantro, cinnamon, citric acid, cloves,coconut shredded, coriander, corn oil, corn starch, cream of tartar,cubeb berries, cumin, curry, dextrose, dill, enzymes, fennel, fenugreek,file powder, garlic powder, ginger, grapefruit peel, green peppercorns,honey, horseradish powder, juniper berries, kaffir lime, lavender, lemongrass powder, lemon peel, lime peel, long pepper, marjoram, molasses,mustard, natural smoke flavor, nigella seeds, nutmeg, onion powder,orange peel, oregano, paprika, parsley, poppy seed, powdered cheese, redpepper, rose petals, rosemary, saffron, sage, salt, savory, sesame seed,star anise, sugar, sugar maple, sumac, tamarind, tangerine peel,tarragon, tetrahydrocannabinol, thyme, tomatillo powder, tomato powder,torula yeast, turmeric, vanilla extract, wasabi powder, whey, whitepeppercorns, yeast extract, and yeast.

In embodiments, the flavoring machine (F12) provides intimate contactbetween the flavoring (F18) and the cooked extrudate (E18) to form aflavored cooked extrudate (F10)

In embodiments, the flavoring machine (F12) provides intimate contactbetween the flavoring (F18) and the cooked multifunctional flour mixture(E18A) to form a flavored multifunctional flour mixture (F10A). Inembodiments, the tumbler (F13) rotates and provides intimate contactbetween the flavoring (F18) and the cooked extrudate (E18) to form aflavored cooked extrudate (F10) or a flavored multifunctional flourmixture (F10A). The flavoring machine (F12) has a flavored cookedextrudate output (F19) for discharging the flavored cooked extrudate(F10) or flavored multifunctional flour mixture (F10A). In embodiments,the tumbler (F13) rotates at a revolution per minute (RPM) ranging frombetween: 3 RPM to 4 RPM; 4 RPM to 5 RPM; 6 RPM to 7 RPM; 7 RPM to 8 RPM;8 RPM to 9 RPM; 9 RPM to 10 RPM; 10 RPM to 11 RPM; 11 RPM to 12 RPM; 13RPM to 14 RPM; 14 RPM to 15 RPM; 15 RPM to 16 RPM; 16 RPM to 17 RPM; 17RPM to 18 RPM; 18 RPM to 19 RPM; 19 RPM to 20 RPM.

In embodiments, the flavored multifunctional flour mixture (F10A) is aflavored cooked extrudate (F10). A conveyor (F20) is equipped to acceptthe flavored cooked extrudate (F10) from the flavored cooked extrudateoutput (F19). The conveyor (F20) may be mechanical, pneumatic, airoperated, an elevating conveyor, conveyor belt, drag-chain conveyor, orany conceivable device to transport flavored multifunctional flourmixture (F10) away from the flavoring machine (F12). The conveyor (F20)may be equipped with a metal detector (F21). The metal detector (F21)may be an electronic instrument which detects the presence of metalwithin the flavored multifunctional flour mixture (F10A).

FIG. 14G

FIG. 14G shows one non-limiting embodiment of a biocatalyst mixingmodule (14G) that is configured to mix insects, water, biocatalyst, andoptionally acid to create an insect liquid biocatalyst mixture (G09).

FIG. 14G shows one non-limiting embodiment of a biocatalyst mixingmodule (14G) that includes a first water treatment unit (G10), a secondwater treatment unit (G11), and a third water treatment unit (G12), thatprovide a third contaminant depleted water (G13) to the interior (G14)of a mixing tank (G15). The mixing tank (G15) mixes a water supply (C16)with insects and biocatalyst. In embodiments, the insects introduced tothe mixing tank (G15) may be ground insects or whole insects. Inembodiments, the first water treatment unit (G10), a second watertreatment unit (G11), and a third water treatment unit (G12) areoptional. In embodiments, only one of the first water treatment unit(G10), second water treatment unit (G11), or third water treatment unit(G12) may be used. In embodiments, two of the first water treatment unit(G10), second water treatment unit (G11), or third water treatment unit(G12) may be used. In embodiments, a water supply (C16) is provided tothe interior (G14) of the mixing tank (G15).

In embodiments, the insects introduced to the mixing tank (G15) may be:(a) ground separated insects (1500) provided by the grinder (1250); (b)separated insects (334) from the separated insect conveyor (328); (c)insects (225) evacuated from the first feeding chamber (FC1) via theinsect evacuation output (205); (d) insects (225) evacuated from thefirst feeding chamber (FC1) via the insect evacuation output (205) andfeeding chamber exit conduit (302); and/or (e) insects removed from thefirst feeding chamber (FC1) via the conveyor output (249).

In embodiments, the insects introduced to the mixing tank (G15) may behave an insect bulk density ranging from between about 3.5 pounds percubic foot to about 14.999 pounds per cubic foot or a ground insect bulkdensity ranging from between about 15 pounds per cubic foot to about 50pounds per cubic foot.

The whole insects (G07) or ground insects (G08) introduced to the mixingtank (G15) may be a weighed. In embodiments, the whole insects (G07)introduced to the mixing tank (G15) may be have an insect bulk densityranging from between about 3.5 pounds per cubic foot to about 14.999pounds per cubic foot. In embodiments, the ground insects (G08) have aground insect bulk density ranging from between about 15 pounds percubic foot to about 50 pounds per cubic foot.

The insect liquid biocatalyst mixture (G09) is transferred from themixing tank (G15) to the exoskeleton separation module (14H) of FIG.14H. In embodiments, the insect liquid biocatalyst mixture (G09) istransferred and pressurized using a pump (G18) from the mixing tank(G15) to the exoskeleton separation module (14H) of FIG. 14H. Inembodiments, the insect liquid biocatalyst mixture (G09) is transferredand pressurized using a screw auger (G19) from the mixing tank (G15) tothe exoskeleton separation module (14H) of FIG. 14H.

FIG. 14G depicts the first water treatment unit (G10) to include acation, a second water treatment unit (G11) to include an anion, and athird water treatment unit (G13) to include a membrane. A first waterpressure sensor (G20) is positioned on the water input conduit (G21)that is introduced to the first input (G22) to the first water treatmentunit (G10). In embodiments, a filter (G23), activated carbon (G24),and/or an adsorbent (G25), are positioned on the water input conduit(G21) prior to introducing the water supply (G16) to the first watertreatment unit (G10). The water supply (G16) may be considered acontaminant-laden water (G26) that includes positively charged ions,negatively charged ions, and undesirable compounds. The positivelycharged ions are comprised of one or more from the group consisting ofcalcium, magnesium, sodium, and iron. The negatively charged ions arecomprised of one or more from the group consisting of iodine, chloride,and sulfate. The undesirable compounds are comprised of one or more fromthe group consisting of dissolved organic chemicals, viruses, bacteria,and particulates.

A first contaminant depleted water (G27) is discharged by the firstwater treatment unit (G10) by a first output (G28). The firstcontaminant depleted water (G27) may be a positively charged iondepleted water (G29). The first contaminant depleted water (G27) is thentransferred to the second water treatment unit (G11) via a second input(G30). A second contaminant depleted water (G31) is discharged by thesecond water treatment unit (G11) by a second output (G32). The secondcontaminant depleted water (G31) may be a negatively charged iondepleted water (G33). The second contaminant depleted water (G31) isthen transferred to the third water treatment unit (G12) via a thirdinput (G34). A third contaminant depleted water (G13) is discharged bythe third water treatment unit (G12) by a third output (G35). The thirdcontaminant depleted water (G13) may be an undesirable compoundsdepleted water (G36). The third contaminant depleted water (G13) is thentransferred to the interior (G14) of a mixing tank (G15) via a watersupply conduit (G37) and water input (G38). In embodiments, a diptube(G38A) is provided to introduce water to beneath the liquid level of thecontents within the interior (G14) of the mixing tank (G15).

Within the interior (G14) of a mixing tank (G15), the water is mixedwith insects and biocatalyst. In embodiments, a cation (G39), an anion(G40), and a polishing unit (G41), are positioned on the water supplyconduit (G37) in between the third water treatment unit (G12) and thewater input (G38) of the mixing tank (G15). The polishing unit (G41) maybe any type of conceivable device to improve the water quality such asan ultraviolet unit, ozone unit, microwave unit, filter, or the like.

In embodiments, water supply valve (G42) is positioned on the watersupply conduit (G37) in between the third water treatment unit (G12) andthe water input (G38) of the mixing tank (G15). The water supply valve(G42) is equipped with a controller (G43) that inputs or outputs asignal from a computer (COMP). In embodiments, the mixing tank (G15) isequipped with a high-level sensor (G44) and a low-level sensor (G45).The high-level sensor (G44) is used for detecting a high level and thelow-level sensor (G45) is used for detecting a low level. The high-levelsensor (G44) is configured to output a signal to the computer (COMP)when the high-level sensor (G44) is triggered by a high level of liquidwithin the mixing tank (G15). The low-level sensor (G45) is configuredto output a signal to the computer (COMP) when the low-level sensor(G45) is triggered by a low level of liquid within the mixing tank(G15).

In embodiments, when the low-level sensor (G45) sends a signal to thecomputer (COMP), the water supply valve (G42) on the water supplyconduit (G37) is opened and introduces water into the mixing tank (G15)until the high-level sensor (G44) is triggered thus sending a signal tothe computer (COMP) to close the water supply valve (G42). This levelcontrol loop including the high-level sensor (G44) for detecting a highlevel and a low-level sensor (G45) for detecting a lower level may becoupled to the operation of the water supply valve (G42) for introducinga water supply (G16) through a first water treatment unit (G10), asecond water treatment unit (G11), and a third water treatment unit(G12), to provide a third contaminant depleted water (G13) to theinterior (G14) of a mixing tank (G15).

The mixing tank (GC15) may be placed on a load cell (G46) for measuringthe mass of the tank. The mixing tank (G15) may be equipped with a mixer(G47) for mixing water with insects and biocatalyst. The insects andbiocatalyst may be introduced to the interior (G14) of the mixing tank(G15) via an input (G51). The mixer (G47) may be of an auger or bladetype that is equipped with a motor (G48). The mixing tank (G15) has aninsect liquid biocatalyst mixture output (G49) that is connected to atransfer conduit (G50).

The transfer conduit (G50) is connected at one end to the insect liquidbiocatalyst mixture output (G49) of the mixing tank (G15) and at anotherend to a supply pump (G18) or a screw auger (G19). The supply pump (G18)or a screw auger (G19) provides a pressurized insect liquid biocatalystmixture (G09B) to the exoskeleton separation module (14H) of FIG. 14H.

In embodiments, a flow sensor (G51) and/or a flow totalizer (G52) may beinstalled on the water supply conduit (G37) to determine the mass orvolume of water that is sent to the interior (G14) of the mixing tank(G15). In embodiments, the mixing tank (G15) is equipped with a heatexchanger (G53) to heat the mixture of water, biocatalyst, and insects.The heat exchanger (G53) may be electrically heated or provided with aheat transfer medium such as a source of steam or hot oil.

The mixing tank (G15) may have a heating jacket (G53J) to serve thepurpose of the heat exchanger (G53). The mixing tank (G15) with aheating jacket (G53J) is a vessel that is designed for controlling thetemperature of its contents, by using a heating jacket around the vesselthrough which a heat transfer medium (e.g.—steam) is circulated. Theheating jacket (G53J) is a cavity external to the interior (G14) of themixing tank (G15) that permits the uniform exchange of heat between theheat transfer medium circulating in it and the walls of the mixing tank(G15). FIG. 14G shows the heating jacket (G53J) installed over a portionof the mixing tank (G15) creating an interior (G53J-1) having an annularspace within which a heat transfer medium flows.

The heating jacket (G53J) has a heat transfer medium inlet (G90) and aheat transfer medium outlet (G91). Steam (G92) is introduced to the heattransfer medium inlet (G90). Steam condensate (G93) is discharged fromthe heat transfer medium outlet (G91). Steam (G92) is introduced to theheat transfer medium inlet (G90) of the heating jacket (G53J) of themixing tank (G15) via a steam inlet conduit (G94). The steam inletconduit (G94) is connected to the heat transfer medium inlet (G90) andis configured to transfer steam to the interior (G53J-1) of the heatingjacket (G53J). A steam supply valve (G95) is interposed on the steaminlet conduit (G94). The steam supply valve (G95) is equipped with acontroller (G96) that inputs and outputs a signal (G97) to the computer(COMP). In embodiments, the steam supply valve (G95) is positioned toregulate the mass of heat transfer medium that leaves the heating jacket(G53J) via the discharged from the heat transfer medium outlet (G91).

In embodiments, a temperature sensor (G54) measures the temperature ofthe contents within the interior (G14) of the mixing tank (G15). Thetemperature sensor (G54) is configured to output a signal (G55) to thecomputer (COMP). A pre-determined setpoint for the mixing tank (G15)temperature sensor (G54) may be inputted to the computer (COMP). Inresponse to the pre-determined setpoint, the computer (COMP) regulatesthe modulation of the steam supply valve (G95). The preferred modulationrange of the steam supply valve (G95) ranges from 33% open to 66% open.In embodiments, the preferred modulation range of the steam supply valve(G95) ranges from: 5% open to 10% open; 10% open to 15% open; 15% opento 20% open; 20% open to 30% open; 30% open to 40% open; 40% open to 50%open; 50% open to 60% open; 60% open to 70% open.

In embodiments, the mixing tank (G15) has a plurality of baffles (G55A,G55B) that are positioned within the interior (G14). Each baffle (G55A,G55B) is configured to promote mixing and increase heat transfer andchemical reaction rate of the biocatalyst with the insects.

The pressure drop across the steam supply valve (G95) ranges frombetween: 1 pound per square inch (PSI) to 2 PSI; 2 pounds per squareinch (PSI) to 5 PSI; 5 pounds per square inch (PSI) to 10 PSI; 10 poundsper square inch (PSI) to 20 PSI; 20 pounds per square inch (PSI) to 40PSI; 40 pounds per square inch (PSI) to 60 PSI; 60 pounds per squareinch (PSI) to 80 PSI; 80 pounds per square inch (PSI) to 100 PSI; 100pounds per square inch (PSI) to 125 PSI; 125 pounds per square inch(PSI) to 150 PSI; 150 pounds per square inch (PSI) to 200 PSI.

The velocity of steam in the steam inlet conduit (G94) ranges from: 35feet per second to 45 feet per second; 45 feet per second to 55 feet persecond; 55 feet per second to 65 feet per second; 65 feet per second to75 feet per second; 75 feet per second to 85 feet per second; 85 feetper second to 95 feet per second; 95 feet per second to 105 feet persecond; 105 feet per second to 115 feet per second; 115 feet per secondto 125 feet per second; 125 feet per second to 135 feet per second; 135feet per second to 145 feet per second; 145 feet per second to 155 feetper second; 155 feet per second to 175 feet per second. The velocity ofsteam condensate discharged from the heat transfer medium outlet (G91)is less than 3 feet per second.

In embodiments, the heat transfer medium inlet (G90) is comprised of oneor more from the group consisting of: a Class 150 flange, a Class 300flange, sanitary clamp fitting, national pipe thread, or compressionfitting. In embodiments, the heat transfer medium outlet (G91) iscomprised of one or more from the group consisting of: a Class 150flange, a Class 300 flange, sanitary clamp fitting, national pipethread, or compression fitting. In embodiments, the mixing tank (G15) iscomprised of stainless steel or carbon steel and may be ceramic orglass-lined. In embodiments, the heating jacket (G53J) is comprised ofstainless steel or carbon steel and may be ceramic or glass-lined.

In embodiments, the temperature of the water, insect, and biocatalystmixture within the interior (G14) of the mixing tank (G15) ranges frombetween: 50 degrees F. to 60 degrees F.; 60 degrees F. to 70 degrees F.;70 degrees F. to 80 degrees F.; 80 degrees F. to 90 degrees F.; 90degrees F. to 100 degrees F.; 100 degrees F. to 110 degrees F.; 110degrees F. to 120 degrees F.; 120 degrees F. to 130 degrees F.; 130degrees F. to 140 degrees F.; 140 degrees F. to 150 degrees F.; 150degrees F. to 160 degrees F.; 160 degrees F. to 170 degrees F.; 170degrees F. to 180 degrees F.; 180 degrees F. to 190 degrees F.; 190degrees F. to 200 degrees F.; 200 degrees F. to 212 degrees F.

In embodiments, the water, insect, and biocatalyst mixture may mixedwithin the interior (G14) of the mixing tank (G15) ranges from between:5 minutes to 10 minutes; 10 minutes to 20 minutes; 20 minutes to 30minutes; 30 minutes to 40 minutes; 40 minutes to 50 minutes; 50 minutesto 1 hour; 1 hour to 1.5 hours; 1.5 hour to 2 hours; 2 hour to 3 hours;3 hour to 4 hours; 4 hour to 5 hours; 5 hour to 6 hours; 6 hour to 12hours; 12 hour to 18 hours; 18 hour to 24 hours; 1 day to 2 days; 2 daysto 3 days; 3 days to 4 days; 4 days to 5 days; 5 days to 1 week.

In embodiments, the mass of water, biocatalyst, or insects within themixing tank (G15) can be measured via the load cell (G46). Inembodiments, water can be added to the mixing tank (G15) and the mass ofwater is measured, following by adding the insects and/or biocatalyst tothe interior (G14) of the mixing tank (G15) to know the mass of thetotal mixture. The contents within the mixing tank (G15) can be mixedwith the mixer and heated.

Whole Insect Distribution Module (14G1)

FIG. 14G displays a whole insect distribution module (14G1) including aninsect tank (G55) that is configured to accept whole insects (G56). Thewhole insects (G56) may be: (a) separated insects (334) from theseparated insect conveyor (328), (b) insects (225) evacuated from thefirst feeding chamber (FC1) via the insect evacuation output (205), (c)insects (225) evacuated from the first feeding chamber (FC1) via theinsect evacuation output (205) and feeding chamber exit conduit (302),and/or, (d) insects removed from the first feeding chamber (FC1) via theconveyor output (249), (e) transported though interstate commerce via atleast one vehicle having three or more axles and having an engine, (f)transported though interstate commerce via at least one vehicle havingtwo axles and having an internal combustion engine or battery powered.

The insect tank (G55) has an interior (G57), an insect input (G58), aninsect conveyor (G59), and an insect conveyor output (G60). The insecttank (G55) accepts whole insects (G56) to the interior (G57) andregulates and controls an engineered amount of whole insects (G56)downstream to be mixed in the mixing tank (G15). The insect conveyor(G59) has an integrated insect mass sensor (G61) that is configured toinput and output a signal (G61A) to the computer (COMP). The insectconveyor motor (G62) has a controller (G63) that is configured to inputand output a signal (G64) to the computer (COMP). The insect mass sensor(G61), insect conveyor (G59), and insect conveyor motor (G62) arecoupled so as to permit the conveyance, distribution, or output of aprecise flow of whole insects (G56) via a whole insect transfer line(G65).

Ground Insect Distribution Module (14G2)

FIG. 14G displays a ground insect distribution module (14G2) includingan insect tank (G66) that is configured to accept ground insects (G67).The ground insects (G67) may be: (a) ground separated insects (1500)provided by the grinder (1250), or (b) insects purchased throughinterstate commerce, (c) transported though interstate commerce via atleast one vehicle having three or more axles and having an internalcombustion engine, (d) transported though interstate commerce via atleast one vehicle having two axles and having an internal combustionengine or battery powered.

The insect tank (G66) has an interior (G68), an insect input (G69), aninsect conveyor (G70), and an insect conveyor output (G71). The insecttank (G66) accepts ground insects (G67) to the interior (G68) andregulates and controls an engineered amount of ground insects (G67)downstream to be mixed in the mixing tank (G15). The insect conveyor(G70) has an integrated insect mass sensor (G72) that is configured toinput and output a signal (G73) to the computer (COMP). The insectconveyor motor (G74) has a controller (G75) that is configured to inputand output a signal (G76) to the computer (COMP). The insect mass sensor(G72), insect conveyor (G70), and insect conveyor motor (G74) arecoupled so as to permit the conveyance, distribution, or output of aprecise flow of ground insects (G67) via a ground insect transfer line(G77).

Biocatalyst Distribution Module (14G3)

FIG. 14G displays a biocatalyst mixing module (14G3) including abiocatalyst tank (G78) that is configured to accept at least onebiocatalyst (G79). The biocatalyst (G79) may be comprised of one or morefrom the group consisting of an enzyme, casein protease, atreptogrisinA, flavorpro, peptidase, protease A, protease, aspergillus oryzae,bacillus subtilis, bacillus licheniformis, aspergillus niger,aspergillus melleus, aspergilus oryzae, papain, carica papaya,bromelain, and ananas comorus stem, and mixtures of two and three andfour and more. In embodiments, mixing of the biocatalyst (G79) isoptional.

The biocatalyst tank (G78) has an interior (G80), a biocatalyst input(G81), a biocatalyst conveyor (G82), and a biocatalyst conveyor output(G83). The biocatalyst tank (G78) accepts biocatalyst (G79) to theinterior (G80) and regulates and controls an engineered amount ofbiocatalyst (G79) downstream to be mixed in the mixing tank (G15). Thebiocatalyst conveyor (G82) has an integrated biocatalyst mass sensor(G84) that is configured to input and output a signal (G85) to thecomputer (COMP). The biocatalyst conveyor motor (G86) has a controller(G87) that is configured to input and output a signal (G88) to thecomputer (COMP). The biocatalyst mass sensor (G84), biocatalyst conveyor(G82), and biocatalyst conveyor motor (G86) are coupled so as to permitthe conveyance, distribution, or output of a precise flow of biocatalyst(G79) via a biocatalyst transfer line (G89). In embodiments, thebiocatalyst transfer line (G89) has a diameter that ranges from: 0.5inches to 0.75 inches, 0.75 inches to 1 inch, 1 inch to 1.5 inches, 2inches to 3 inches, 3 inches to 4 inches.

Acid Distribution Module (14G3′)

FIG. 14G displays an acid mixing module (14G3′) including an acid tank(G78′) that is configured to accept at least one acid (G79′). The acid(G79′) may be comprised of one or more from the group consisting of anacid, abscic acid, acetic acid, ascorbic acid, benzoic acid, citricacid, formic acid, fumaric acid, hydrochloric acid, lactic acid, malicacid, nitric acid, organic acids, phosphoric acid, potassium hydroxide,propionic acid, salicylic acid, sulfamic acid, sulfuric acid, andtartaric acid.

In embodiments, whole insects (G56) and/or ground insects (G67) have apH that is greater than 7. In embodiments, whole insects (G56) and/orground insects (G67) have a pH that is basic and ranges from greaterthan 7 to less than 8.75. In embodiments, whole insects (G56) and/orground insects (G67) added to the interior (G14) of the mixing tank(G15) is required to lower the pH of the water, insect, biocatalystmixture to a pH that is sufficient for the biocatalyst to digest orhydrolyze the insects. In embodiments, addition of an acid (G79′) to theinterior (G14) of the mixing tank (G15) is required to maintain theliquid mixture of biocatalyst, insects, and water within the mixing tank(G15) to be at a desired range from within 6.25 to 7.5.

The acid tank (G78′) has an interior (G80′), an acid input (G81′), anacid conveyor (G82′), and an acid conveyor output (G83′). The acid tank(G78′) accepts acid (G79′) to the interior (G80′) and regulates andcontrols an engineered amount of acid (G79′) downstream to be mixed inthe mixing tank (G15).

The acid conveyor (G82′) has an integrated acid mass sensor (G84′) thatis configured to input and output a signal (G85′) to the computer(COMP). The acid conveyor motor (G86′) has a controller (G87′) that isconfigured to input and output a signal (G88′) to the computer (COMP).The acid mass sensor (G84′), acid conveyor (G82′), and acid conveyormotor (G86′) are coupled so as to permit the conveyance, distribution,or output of a precise flow of acid (G79′) via an acid transfer line(G89′). In embodiments, the acid transfer line (G89′) has a diameterthat ranges from: 0.5 inches to 0.75 inches, 0.75 inches to 1 inch, 1inch to 1.5 inches, 2 inches to 3 inches, 3 inches to 4 inches.

In embodiments, the mixing tank (G15) is equipped with a pH sensor (PHG)that is configured to output a signal (PHG′) to the computer (COMP). Inembodiments, the pH sensor (PHG) is used in a control loop with the acidmass sensor (G84′), acid conveyor (G82′), and acid conveyor motor (G86′)to permit output of a precise flow of acid (G79′) to the interior (G14)of the mixing tank (G15) to maintain a predetermined pH within themixing tank (G15).

FIG. 14G shows the whole insects (G56), ground insects (G67),biocatalyst (G79), and acid (G79′) introduced to the interior (G14) ofthe mixing tank (G15) via an input (G100). It is not required that thewhole insects (G56), ground insects (G67), biocatalyst (G79), and acid(G79′) are combined into a combined stream (G101) for input (G100) tothe interior (G14) of the mixing tank (G15). It is apparent to thoseskilled in the art to which it pertains that each whole insects (G56),ground insects (G67), biocatalyst (G79), and acid (G79′) can have theirown input to the interior (G14) of the mixing tank (G15) as well.

In embodiments, another alternate liquid (G102) may be added to theinterior (G14) of the mixing tank (G15) to replace or be mixed with thesource of water (01). In embodiments, the alternate liquid (G102) arecomprised of one or more from the group consisting of alcohol,diglycerides, esters, ethanol, ethyl acetate, glycerin, glycerol,hexane, hydrocarbon, insect lipids, isopropyl alcohol, methanol,Monoglycerides, oil, and solvent.

FIG. 14H

FIG. 14H shows one non-limiting embodiment of an exoskeleton separationmodule (14H) that is configured to remove the exoskeleton containedwithin the insect liquid biocatalyst mixture (G09).

FIG. 14H shows the exoskeleton separation module (14H) configured toremove exoskeleton from insects that are contained within the insectliquid biocatalyst mixture (G09). In embodiments, where the biocatalyst(G79) within the biocatalyst mixing module (14G) is optional, theexoskeleton separation module (14H) is configured to remove exoskeletonfrom insects that are contained within an insect and liquid mixture(G09A) as depicted in FIG. 14G. In embodiments, exoskeleton is chitin.In embodiments, exoskeleton is a long-chain polymer of anN-acetylglucosamine, a derivative of glucose. In embodiments, theexoskeleton is provided to the insects to eat within the insect feedingchamber (FC). In embodiments, the exoskeleton removed in the exoskeletonseparation module (14H) is provided to the polymer distribution module(1D) within the enhanced feedstock mixing module (1000) as shown in FIG.2.

The insect liquid biocatalyst mixture (G09) or an insect and liquidmixture (G09A) is transferred from the mixing tank (G15) to theexoskeleton separation module (14H) of FIG. 14H via a transfer conduit(G50). FIG. 14H displays the exoskeleton separation module (14H)including an exoskeleton separator (H10). In embodiments, theexoskeleton separator (H10) is a filter (H11) having at least one sidewall (H65). In embodiments, the filter (H11) is cylindrical. Inembodiments, the filter (H11) is a candle filter (H12) that has at leastone filter element (H13) contained within its interior (H64). Inembodiments, the filter (H11) has a top (H14) and a bottom (H15). FIG.14H shows a separator input (H16) positioned on the side wall (H65) ofthe exoskeleton separator (H10). The separator input (H16) is configuredto introduce an exoskeleton-laden insect mixture (H17) to the interior(H64) of the filter (H11). In embodiments, the insect liquid biocatalystmixture (G09) or an insect and liquid mixture (G09A) may be consideredan exoskeleton-laden insect mixture (H17).

A supply valve (H61) equipped with a controller (H62) and configured toinput and output a signal (H63) to the computer (COMP) is positioned onthe transfer conduit (G50) in between the mixing tank (G15) of FIG. 14Gand the separator input (H16) positioned on the side wall (H65) of theexoskeleton separator (H10).

The filter (H11) has a first output (H18) positioned on the top (H14).The first output (H18) is configured to discharge anexoskeleton-depleted insect liquid mixture (H19) via anexoskeleton-depleted mixture conduit (H20). A discharge valve (H21)equipped with a controller (H22) and configured to input and output asignal (H23) to the computer (COMP) is positioned on theexoskeleton-depleted mixture conduit (H20). The filter (H11) isconfigured to remove exoskeleton (H46) from either the insect liquidbiocatalyst mixture (G09) or the insect and liquid mixture (G09A) toform an exoskeleton-depleted insect liquid mixture (H19). Theexoskeleton-depleted insect liquid mixture (H19) has a reduced amount ofexoskeleton (H46) relative to the insect liquid biocatalyst mixture(G09) or an insect and liquid mixture (G09A).

In embodiments, a flow sensor (H24) and a secondary filter (H25) areboth installed on the exoskeleton-depleted mixture conduit (H20). Theflow sensor (H24) can be an electronic instrument, but a manualpaddle-wheel type flow sensor or a totalizer are preferred. Alternately,the flow sensor (H24) may be of a rotameter, variable-area flow meter, abullseye type flow sensor, or a sight-glass type sensor and configuredto allow one to visually observe the clarity, and lack of exoskeletonsolids within the exoskeleton-depleted insect liquid mixture (H19). Thesecondary filter (H25) is used as an emergency filter to preventcontamination of the downstream exoskeleton-depleted insect liquidmixture tank (H26). The secondary filter (H25) is preferably installedto mitigate any risk of contamination downstream in the event that thefilter element (H13) becomes ruptured and solid exoskeleton particlesare transferred via the exoskeleton-depleted mixture conduit (H20) andinto the interior (H27) of the exoskeleton-depleted insect liquidmixture tank (H26).

An exoskeleton-depleted insect liquid mixture tank (H26) is connected tothe exoskeleton-depleted mixture conduit (H20) and configured to receivethe exoskeleton-depleted insect liquid mixture (H19) from theexoskeleton separator (H10). The exoskeleton-depleted mixture conduit(H20) is connected at one end to the first output (H18) of theexoskeleton separator (H10) and at another end to the input (H28) of theexoskeleton-depleted insect liquid mixture tank (H26).

The exoskeleton-depleted insect liquid mixture tank (H26) has an input(H28) through which an exoskeleton-depleted insect liquid mixture (H19)is received to the interior (H27). A diptube (H29) may be installed onthe input (H28) of the exoskeleton-depleted insect liquid mixture tank(H26) to introduce the exoskeleton-depleted insect liquid mixture (H19)to the interior (H27) beneath the liquid level. An upper level sensor(H30) and lower level sensor (H31) are installed on theexoskeleton-depleted insect liquid mixture tank (H26). A mixer (H32)with a motor (H33) may also be installed on the exoskeleton-depletedinsect liquid mixture tank (H26) to provide agitation of the liquidcontents within the interior (H27). A heat exchanger (H34) may beinstalled to heat a portion of the exoskeleton-depleted insect liquidmixture (H19) within the exoskeleton-depleted insect liquid mixture tank(H26). A temperature sensor (H35) may be installed on theexoskeleton-depleted insect liquid mixture tank (H26). A mass sensor(H36) may be installed on the exoskeleton-depleted insect liquid mixturetank (H26).

The exoskeleton-depleted insect liquid mixture tank (H26) has an output(H37) that is configured to discharge an exoskeleton-depleted insectliquid mixture (H39) from the interior (H27). An exoskeleton-depletedinsect liquid mixture conduit (H38) is connected to the output (H37) andconfigured to transfer exoskeleton-depleted insect liquid mixture (H39)away from the interior (H27) and towards the liquid separation module(LSM) shown in FIGS. 14i and 14J.

A pump (H40) is interposed on the exoskeleton-depleted insect liquidmixture conduit (H38) and configured to pressurize theexoskeleton-depleted insect liquid mixture (H39) to form a pressurizedexoskeleton-depleted insect liquid mixture (H41). A pressure sensor(H42) is installed on the exoskeleton-depleted insect liquid mixtureconduit (H38). In embodiments, the pump (H40) is configured topressurize the exoskeleton-depleted insect liquid mixture (H39) to apressure that ranges from between 10 pounds per square inch (PSI) to 20PSI; 20 PSI to 30 PSI; 30 PSI to 40 PSI; 40 PSI to 50 PSI; 50 PSI to 60PSI; 60 PSI to 70 PSI; 70 PSI to 80 PSI; 80 PSI to 90 PSI; 90 PSI to 100PSI; 100 PSI to 125 PSI; 125 PSI to 150 PSI; 150 PSI to 200 PSI; 200 PSIto 300 PSI; 300 PSI to 500 PSI.

A recirculation conduit (H43) may be positioned on theexoskeleton-depleted insect liquid mixture conduit (H38) and configuredto transport a portion of the pressurized exoskeleton-depleted insectliquid mixture (H41) back to the interior (H27) of theexoskeleton-depleted insect liquid mixture tank (H26). A recirculationfilter (H44) may be positioned on the recirculation conduit (H43) toremove any particulates from the pressurized exoskeleton-depleted insectliquid mixture (H41) before being sent back to the interior (H27) of theexoskeleton-depleted insect liquid mixture tank (H26).

The filter (H11) has a second output (H45) positioned on the bottom(H15). Exoskeleton (H46) may be separated from the insect liquidbiocatalyst mixture (G09) or an insect and liquid mixture (G09A). Aseparated exoskeleton transfer conduit (H47) is connected to the secondoutput (H45) positioned on the bottom (H15) of the filter (H11). Anexoskeleton conveyor (H48) is equipped to receive exoskeleton (H46) fromthe separated exoskeleton transfer conduit (H47).

An exoskeleton drying gas (H49) may be applied to a portion of theexoskeleton (H46) to remove liquid therefrom and form dehydratedexoskeleton (H50). In embodiments, the exoskeleton drying gas (H49) isheated to a temperature ranging from between 80 degrees F. to 90 degreesF.; 90 degrees F. to 100 degrees F.; 100 degrees F. to 110 degrees F.;110 degrees F. to 120 degrees F.; 120 degrees F. to 140 degrees F.; 140degrees F. to 160 degrees F.; 160 degrees F. to 180 degrees F.; 180degrees F. to 200 degrees F.; 200 degrees F. to 250 degrees F.; 250degrees F. to 300 degrees F.; 300 degrees F. to 400 degrees F.

An exoskeleton discharge valve (H51) equipped with a controller (H52)and configured to input and output a signal (H53) to the computer (COMP)is installed on the separated exoskeleton transfer conduit (H47).

A backflush fluid (H54) may be provided to the filter (H11) toregenerate the filter element (H13). FIG. 14H shows the backflush fluid(H54) entering the exoskeleton-depleted mixture conduit (H20) and thenentering the interior (H64) of the filter (H11) via the first output(H18). In embodiments, the backflush fluid (H54) is a liquid. Inembodiments, the backflush fluid (H54) is a gas.

A backflush fluid transfer conduit (H55) is connected to theexoskeleton-depleted mixture conduit (H20) via a connection (H70) inbetween the discharge valve (H21) and the first output (H18). Abackflush fluid supply valve (H56) equipped with a controller (H57) andconfigured to input and output a signal (H58) to the computer (COMP) ispositioned on the backflush fluid transfer conduit (H55). Inembodiments, a backflush fluid pressure regulating valve (H59) with abackflush pressure sensor (H60) is positioned upstream of the backflushfluid supply valve (H56). In embodiments, the backflush fluid pressureregulating valve (H59) may be adjusted to a pressure that is less thanthe rupture pressure of that of the filter element (H13). It ispreferred to counter currently backflush the filter element (H13) bysetting the pressure of the backflush fluid pressure regulating valve(H59) to a pressure of 0.25 PSI to 0.5 PSI; 0.5 PSI to 1.5 PSI; 1.5 PSIto 3 PSI; 3 PSI to 6 PSI; 6 PSI to 9 PSI; 9 PSI to 15 PSI.

The best mode of operation for realizing a continuous filtrate streamdepleted of exoskeleton and encompasses operating the filtration systemin a manner which allows for periodic back flushing of the filterelement cloth surface in-situ by providing a counter-current flow ofbackflush fluid to the filter element. The backwashing dislodges anyaccumulated exoskeleton, in the form of a filter cake, allowing it tosink to the bottom of the filter for removal of the system as a thick,paste-like, filter cake substance.

It is preferred to utilize differential pressure across a filter bundleas the main variable to determine when to undergo a back-flushing cycle,as opposed to using manual predetermined periodic time durationintervals, or using the reduction in flow through the filter bundles asthe variable dictating when to commence filter back flushing,(synonymously termed ‘filter cleaning’, or ‘filter backwashing’,‘in-situ filter cleaning’, or ‘filter surface in-situ regeneration’).Filter element differential pressure between 0.25 and 15 PSI iscommensurate with preferable cake thickness of 20 to 35 millimeters. Incontrast, using manual predetermined periodic time duration intervals asthe sole mechanism to determine when to commence filter cleaning, oftenresults in operational impairment, in that ‘cake bridging’ more readilyoccurs. ‘Cake bridging’ may be described as a large mass of agglomeratedexoskeleton suspended solids filling the spaces between the filterelements and thus posing a challenge to regenerate in-situ, frequentlyrequiring process interruption for physical cleaning and removal of theheavy, gelatinous exoskeleton filter cake.

In-situ filter cleaning may be accomplished by reversing the flow ofliquid or gas through the filter element thereby dislodging exoskeletonfilter cake from the cloth surface thus allowing it to sink to thebottom of the interior of the filter. This affords operations the luxuryof minimizing losses of valuable solvent while draining the filter cakefrom the system.

Filter Operating Procedure

Herein is described the preferred operating procedure for continuousfiltration of exoskeleton. Filtration [step 950] cooperates with thecyclic-batch filter in-situ cleaning steps of: filter element [step952]; filter backflush [step 954]; filter cake sedimentation [step 956];filter cake discharge start [step 958]; filter cake discharge end [step960]; and filtration restart preparation [step 962].

In step 950, (filtration), filtration proceeds and the filter pressuredrop is monitored. As a filtration cycle progresses, solid exoskeletonparticles are deposited onto the surface of the filter element andadhere to its surface until a nominal target differential pressure dropbetween around 0.25 to 15 PSI is attained, which is proportionate to apredetermined thickness of 20 to 35 millimeters. If the filter pressuredrop is lower than the nominal target differential pressure drop, thefiltering cycle continues until the nominal target differential pressuredrop is reached. When a filter has reached its nominal targetdifferential pressure drop, a filter cleaning cycle will commence, whichbegins with step 952 (filter bundle isolation). The sequential stepsencompassing filtration and filter cleaning can be further illuminatedby using FIG. 14H, which visually indicate some of the valve sequencinginvolved, as indicated by open and closed valve positions, illustratedby ‘non-darkened-in valves’ and ‘darkened-in valves’, respectively,wherein: supply valve (H61) is open; discharge valve (H21) is open;backflush fluid supply valve (H56) is closed; exoskeleton dischargevalve (H51) is closed.

When a nominal target pressure drop across a filter is attained, theexoskeleton filter cake material must be dislodged from the filterelement, and thus step 952 (filter isolation) proceeds, which involvesisolating the filter by closing the supply valve (H61) and dischargevalve.

Once both the supply valve (H61) and discharge valve are closed, toisolate the filter, step 954 may proceed. Step 954, (filtratebackflush), involves transferring a backflush fluid (liquid or gas) tobackflush the filter. In embodiments, a typical backflush, in step 954,requires that the backflush fluid supply valve (H56) need be left openfor a duration between: 5 seconds to 10 seconds; 10 seconds to 30seconds; 30 seconds to 1 minute; 1 minute to 5 minutes; 5 minutes to 15minutes; 15 minutes to 30 minutes; 30 minutes to 60 minutes; 60 minutesto 90 minutes.

After the backflush fluid (H54) has been introduced to the filter, andonce the backflush fluid supply valve (H56) has been returned to aclosed position, step 956 may commence. Step 956 (exoskeleton filtercake sedimentation) entails allowing the dislodged exoskeleton filtercake solids to sink to the bottom of the filter.

Step 958 (exoskeleton filter cake discharge start) involves opening theexoskeleton discharge valve (H51) to allow transference of anagglomerated exoskeleton particulate filter cake material from thesystem. The backflush fluid (H54) may be liquid or gas or a combinationof both during Step 958. In embodiments, a gas may be used to dry theexoskeleton and then dislodge the dried exoskeleton from the surface ofthe filter element (H13).

Step 960 (filter cake discharge end) entails closing the exoskeletondischarge valve (H51) since exoskeleton have been discharged from thesystem. After step 960 has transpired, step 962 (filtration restartpreparation) may commence which entails opening the supply valve (H61)and discharge valve (H21) to again commence filtration on theregenerated filter bundle, thus allowing step 950 to commence again,then allowing the filtration and regeneration cycle to repeat itself.

FIG. 14I

FIG. 14I shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from the exoskeleton-depletedinsect liquid mixture (H39) to provide an insect-depleted liquid mixture(I19) and insects (I46).

FIG. 14I shows the liquid separation module (LSM) that is configured toremove liquid from the exoskeleton-depleted insect liquid mixture (H39)or the pressurized exoskeleton-depleted insect liquid mixture (H41).FIG. 14I shows the liquid separation module (LSM) configured to removeliquid from the exoskeleton-depleted insect liquid mixture (H39) that isprovided by the exoskeleton separation module (14H). FIG. 14I shows theliquid separation module (LSM) configured to remove liquid from thepressurized exoskeleton-depleted insect liquid mixture (H41) that isprovided by the exoskeleton separation module (14H). FIG. 14I shows onenon-limiting embodiment of a liquid separation module (LSM) thatincludes a filter (I11). FIG. 14J shows one non-limiting embodiment of aliquid separation module (LSM) that includes an evaporator (J11).

FIG. 14I shows an exoskeleton-depleted insect liquid mixture (H39) or apressurized exoskeleton-depleted insect liquid mixture (H41) transferredto the liquid separation module (LSM) from the exoskeleton separationmodule (14H) shown in FIG. 14H. The exoskeleton-depleted insect liquidmixture (H39) or a pressurized exoskeleton-depleted insect liquidmixture (H41) is transferred from the exoskeleton-depleted insect liquidmixture tank (H26) of FIG. 14H via the exoskeleton-depleted insectliquid mixture conduit (H38).

FIG. 14I displays the liquid separation module (LSM) including a liquidseparator (I10). In embodiments, the liquid separator (I10) is a filter(I11) or a membrane (I11A) having at least one side wall (I65). Inembodiments, the filter (I11) is cylindrical. In embodiments, the filter(I11) is a candle filter (I12) that has at least one filter element(I13) contained within its interior (I64). In embodiments, the filter(I11) has a top (I14) and a bottom (I15). FIG. 14I shows a separatorinput (I16) positioned on the side wall (I65) of the liquid separator(I10). The separator input (I16) is configured to introduce anexoskeleton-depleted insect liquid mixture (H39) or a pressurizedexoskeleton-depleted insect liquid mixture (H41) to the interior (I64)of the filter (I11). In embodiments, the exoskeleton-depleted insectliquid mixture (H39) or pressurized exoskeleton-depleted insect liquidmixture (H41) may be considered a liquid-laden insect mixture (I17).

A supply valve (I61) equipped with a controller (I62) and configured toinput and output a signal (I63) to the computer (COMP) is positioned onthe exoskeleton-depleted insect liquid mixture conduit (H38) in betweenthe exoskeleton-depleted insect liquid mixture tank (H26) of FIG. 14Hand the separator input (I16) positioned on the side wall (I65) of theliquid separator (I10) of FIG. 14I.

The filter (I11) has a first output (I18) positioned on the top (I14).The first output (I18) is configured to discharge an insect-depletedliquid mixture (I19) via an insect-depleted liquid mixture conduit(I20). A discharge valve (I21) equipped with a controller (I22) andconfigured to input and output a signal (I23) to the computer (COMP) ispositioned on the insect-depleted liquid mixture conduit (I20). Thefilter (I11) is configured to remove insects (I46) from either theexoskeleton-depleted insect liquid mixture (H39) or pressurizedexoskeleton-depleted insect liquid mixture (H41) to form aninsect-depleted liquid mixture (I19). The insect-depleted liquid mixture(I19) has a reduced amount of insects (I46) relative to theexoskeleton-depleted insect liquid mixture (H39) or pressurizedexoskeleton-depleted insect liquid mixture (H41).

The filter (I11) has a second output (I45) positioned on the bottom(I15). Insects (I46) may be separated from the exoskeleton-depletedinsect liquid mixture (H39) or pressurized exoskeleton-depleted insectliquid mixture (H41). A separated insect transfer conduit (I47) isconnected to the second output (I45) positioned on the bottom (I15) ofthe filter (I11). An insect conveyor (I48) is equipped to receiveinsects (I46) from the separated insect transfer conduit (I47).

An insect drying gas (I49) may be applied to a portion of the insects(I46) to remove any residual liquid therefrom and form insect andliquid-depleted insects (I50). In embodiments, the insect drying gas(I49) is heated to a temperature ranging from between 80 degrees F. to90 degrees F.; 90 degrees F. to 100 degrees F.; 100 degrees F. to 110degrees F.; 110 degrees F. to 120 degrees F.; 120 degrees F. to 140degrees F.; 140 degrees F. to 160 degrees F.; 160 degrees F. to 180degrees F.; 180 degrees F. to 200 degrees F.; 200 degrees F. to 250degrees F.; 250 degrees F. to 300 degrees F.; 300 degrees F. to 400degrees F.

An insect discharge valve (I51) equipped with a controller (I52) andconfigured to input and output a signal (I53) to the computer (COMP) isinstalled on the separated insect transfer conduit (I47). A backflushfluid (I54) may be provided to the filter (I11) to regenerate the filterelement (I13). FIG. 14I shows the backflush fluid (I54) entering theinsect-depleted liquid mixture conduit (I20) and then entering theinterior (I64) of the filter (I11) via the first output (I18). Inembodiments, the backflush fluid (I54) is a liquid. In embodiments, thebackflush fluid (I54) is a gas.

A backflush fluid transfer conduit (I55) is connected to theinsect-depleted liquid mixture conduit (I20) via a connection (I70) inbetween the discharge valve (I21) and the first output (I18). Abackflush fluid supply valve (IH56) equipped with a controller (I57) andconfigured to input and output a signal (I58) to the computer (COMP) ispositioned on the backflush fluid transfer conduit (I55). Inembodiments, a backflush fluid pressure regulating valve (I59) with abackflush pressure sensor (I60) is positioned upstream of the backflushfluid supply valve (I56). In embodiments, the backflush fluid pressureregulating valve (I59) may be adjusted to a pressure that is less thanthe rupture pressure of that of the filter element (I13). It ispreferred to counter currently backflush the filter element (I13) bysetting the pressure of the backflush fluid pressure regulating valve(I59) to a pressure of 0.25 PSI to 0.5 PSI; 0.5 PSI to 1.5 PSI; 1.5 PSIto 3 PSI; 3 PSI to 6 PSI; 6 PSI to 9 PSI; 9 PSI to 15 PSI.

FIG. 14J

FIG. 14J shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from the exoskeleton-depletedinsect liquid mixture (H39) to produce a vaporized liquid (J22) and astream of liquid-depleted insects (J10).

FIG. 14J shows the liquid separation module (LSM) that is configured toremove liquid from the exoskeleton-depleted insect liquid mixture (H39)or the pressurized exoskeleton-depleted insect liquid mixture (H41) toform a stream of liquid-depleted insects (J10). FIG. 14J shows theliquid separation module (LSM) configured to remove liquid from theexoskeleton-depleted insect liquid mixture (H39) that is provided by theexoskeleton separation module (14H). FIG. 14J shows the liquidseparation module (LSM) configured to remove liquid from the pressurizedexoskeleton-depleted insect liquid mixture (H41) that is provided by theexoskeleton separation module (14H).

FIG. 14J shows one non-limiting embodiment of a liquid separation module(LSM) that includes an evaporator (J11). FIG. 14J shows anexoskeleton-depleted insect liquid mixture (H39) or a pressurizedexoskeleton-depleted insect liquid mixture (H41) transferred to theliquid separation module (LSM) from the exoskeleton separation module(14H) shown in FIG. 14H. The exoskeleton-depleted insect liquid mixture(H39) or a pressurized exoskeleton-depleted insect liquid mixture (H41)is transferred from the exoskeleton-depleted insect liquid mixture tank(H26) of FIG. 14H via the exoskeleton-depleted insect liquid mixtureconduit (H38). FIG. 14J displays the liquid separation module (LSM)including a liquid separator (J10). In embodiments, the liquid separator(I10) is an evaporator (J11) which separates liquid by vaporizing theliquid.

In embodiments, the evaporator (J11) is a wiped-film evaporator (J11A).In embodiments, the evaporator (J11) is comprised of one or more fromthe group consisting of falling film tubular evaporator, rising/fallingfilm tubular evaporator, rising film tubular evaporator, forcedcirculation evaporator, internal pump forced circulation evaporator,plate evaporator, evaporative cooler, multiple-effect evaporator,thermal vapor recompression evaporator, mechanical vapor recompressionevaporator, flash tank, and a distillation column. The evaporator (J11)shown in FIG. 14J is that of a wiped-film evaporator (J11A). Theevaporator (J11) has a vapor inlet (J12), a separator input (J16), aheating jacket (J17), a first output (J18), and a second output (J19).

In embodiments, the evaporator (J11) is electrically heated. Inembodiments, the vapor inlet (J12) is provided with a vapor (J12A) suchas steam. The vapor inlet is connected to a vapor supply conduit (J13).A vapor supply valve (J14) is positioned on the vapor supply conduit(J13). The vapor supply valve (J14) is equipped with a controller (J15A)that is configured to input and output a signal (J15B) to the computer(COMP). In embodiments, the pressure drop across the vapor supply valve(J14) ranges from between 5 PSI to 10 PSI, 15 PSI to 25 PSI, 25 PSI to35 PSI, 35 PSI to 45 PSI, 45 PSI to 55 PSI, 55 PSI to 65 PSI, 65 PSI to75 PSI, 75 PSI to 85 PSI. In embodiments, the vapor supply valve (J14)percent open during normal operation ranges from 10% open to 25% open,25% open to 35% open, 35% open to 45% open, 45% open to 55% open, 55%open to 65% open, 65% open to 75% open, 75% open to 80% open.

A separated vapor transfer conduit (J20) is connected to the firstoutput (J18) and is configured to transfer vaporized liquid (J22) fromthe evaporator (J11) to a condenser (J26). The condenser (J26) has avaporized liquid input (J25) that is configured to transfer thevaporized liquid (J22) from the separated vapor transfer conduit (J20)to the condenser (J26). The condenser (J26) is configured to acceptvaporized liquid (J22) from the evaporator (J11) and condense the liquidinto condensate (J27). Condensate (J27) is discharged from the condenser(J26) via a condenser condensate output (J30).

The condenser is connected to a vacuum system (J32) via a gas/vaportransfer conduit (J33). Gas/vapor (J35) is evacuated from the condenser(J27) via a gas/vapor discharge (J37). The gas/vapor (J35) transferredfrom the condenser to the vacuum system (J32) may be comprised of one ormore from the group consisting of carbon dioxide, nitrogen, air, steam,water vapor, and non-condensables. The vacuum system (J32) may be anyconceivable system configured to draw a vacuum on the condenser (J26).In embodiments, the vacuum system (J32) is that of a liquid-ring vacuumpump. A portion of the gas/vapor (J35) may be in turn condensed withinthe vacuum system (J26). A portion of the gas/vapor (J35) may bedischarged from the vacuum system (J26) via a gas/vapor transfer line(J39).

The condenser (J26) is provided with a cooling water input (J36) and acooling water output (J40). The cooling water input (J36) is configuredto accept a cooling water supply (J38) and the cooling water output(J40) is configured to discharge a cooling water return (J42). Thecooling water supply (J38) is configured to reduce the temperature ofthe vaporized liquid (J22) within the condenser (J26) to convert thevapor into a liquid condensate (J27).

The evaporator (J11) has an evaporator condensate output (J24) forevacuating condensate (J41) from the heating jacket (J17). Thecondensate (J41) discharged via the evaporator condensate output (J24)was provided to the evaporator heating jacket (J17) as the vapor (J12A)or steam. The heating jacket (J17) accepts a source of vapor (J12A), andevaporates liquid from the exoskeleton-depleted insect liquid mixture(H39) or the pressurized exoskeleton-depleted insect liquid mixture(H41) to form vaporized liquid (J22) that is discharged from theevaporator (J11) and sent to the condenser (J26).

In embodiments, the evaporator (J11) takes the form of a wiped-filmevaporator (J11A). In embodiments, the wiped-film evaporator (J11A) hasa motor (J42) and a wiper (J44). In embodiments, the motor (J42) andwiper (J44) act together to wipe at least one heat transfer surfacewithin the evaporator (J11).

The separator input (J16) is configured to introduce anexoskeleton-depleted insect liquid mixture (H39) or a pressurizedexoskeleton-depleted insect liquid mixture (H41) to the evaporator(J11). In embodiments, the exoskeleton-depleted insect liquid mixture(H39) or pressurized exoskeleton-depleted insect liquid mixture (H41)may be considered a liquid-laden insect mixture (117). The evaporatorvaporizes liquid from within the exoskeleton-depleted insect liquidmixture (H39) or pressurized exoskeleton-depleted insect liquid mixture(H41) to produce a vaporized liquid (J22) and a stream ofliquid-depleted insects (J10).

FIG. 15

FIG. 15 shows a simplistic diagram illustrating a plurality of feedingchambers (FC1, FC2, FC3) of an insect feeding module (2000) integratedwithin one common separator (300) of an insect evacuation module (3000).

FIG. 15 shows an insect feeding module (2000) comprised of threeseparate feeding chambers (FC1, FC2, FC3) including a first feedingchamber (FC1), second feeding chamber (FC2), and a third feeding chamber(FC3). Each feeding chamber (FC1, FC2, FC3) may include the non-limitingembodiments of those previously described or those described below. Itis well established that the claims of the patent serve an importantpublic notice function to potential competitors—enabling them to notonly determine what is covered, but also what is not covered—by thepatent. And a number of Federal Circuit decisions have emphasized theimportance of discerning the patentee's intent—as expressed in thespecification—in construing the claims of the patent. The presentdisclosure includes several independently meritorious inventive aspectsand advantages related feeding and evacuating insects by use of at leastone insect feeding module (2000) integrated at least one separator (300)of an insect evacuation module (3000) and to the notion that eachfeeding chamber (FC1, FC2, FC3) has a feeding chamber insect evacuationoutput (205A, 205B, 205C) that is connected to the separator (300) ofthe insect evacuation module (3000).

First Feeding Chamber (FC1)

The first feeding chamber (FC1) has a first feeding chamber insectevacuation output (205A) or a feeding chamber 1 insect evacuation port(1FC) that is in fluid communication with the insect and gas mixtureinput (303) of the separator (300). A first feeding chamber exit conduit(302A) is connected at one end to the first feeding chamber (FC1) and atanother and to a common entry conduit (CEC). The common entry conduit(CEC) is connected at one end to the first feeding chamber exit conduit(302A) and at another end to the insect and gas mixture input (303) ofthe separator (300). A feeding chamber 1 evacuation valve (VV1) ininterposed in the first feeding chamber exit conduit (302A). The feedingchamber 1 evacuation valve (VV1) is equipped with a with a controller(CV1) that is configured to input and output a signal (XV1) to thecomputer (COMP). The first feeding chamber exit conduit (302A) has afirst feeding chamber evacuation line first diameter (D1A) and a firstfeeding chamber evacuation line reducer (VR1) which merges into a firstfeeding chamber evacuation line second diameter (D1B). In embodiments,the first feeding chamber evacuation line first diameter (D1A) isgreater than the first feeding chamber evacuation line second diameter(D1B). In embodiments, the first feeding chamber evacuation line firstdiameter (D1A) is less than the first feeding chamber evacuation linesecond diameter (D1B).

In embodiments, the first feeding chamber evacuation line first diameter(D1A) ranges in size from: between about 1 inch and about 2 inches;between about 2 inches and about 3 inches; between about 3 inches andabout 4 inches; between about 4 inches and about 5 inches; between about5 inches and about 6 inches; between about 6 inches and about 7 inches;between about 7 inches and about 8 inches; between about 8 inches andabout 9 inches; between about 9 inches and about 10 inches; betweenabout 10 inches and about 11 inches; between about 11 inches and about12 inches; between about 12 inches and about 13 inches; between about 13inches and about 14 inches; between about 14 inches and about 15 inches;between about 15 inches and about 16 inches; between about 16 inches andabout 17 inches; between about 17 inches and about 18 inches; betweenabout 18 inches and about 19 inches; between about 19 inches and about20 inches; between about 20 inches and about 21 inches; between about 21inches and about 22 inches; between about 22 inches and about 23 inches;between about 23 inches and about 24 inches; between about 24 inches andabout 25 inches; between about 25 inches and about 26 inches; betweenabout 26 inches and about 27 inches; between about 27 inches and about28 inches; between about 28 inches and about 29 inches; between about 29inches and about 30 inches; between about 30 inches and about 31 inches;between about 31 inches and about 32 inches; between about 32 inches andabout 33 inches; between about 33 inches and about 34 inches; betweenabout 34 inches and about 35 inches; between about 35 inches and about36 inches; between about 36 inches and about 37 inches; between about 37inches and about 38 inches; between about 38 inches and about 39 inches;or, between about 39 inches and about 40 inches; between about 38 inchesand about 39 inches; between about 39 inches and about 40 inches;between about 40 inches and about 50 inches; between about 50 inches andabout 60 inches; between about 60 inches and about 70 inches; betweenabout 70 inches and about 80 inches; between about 80 inches and about90 inches; between about 90 inches and about 100 inches; between about100 inches and about 125 inches; between about 125 inches and about 150inches; or, between about 150 inches and about 200 inches.

In embodiments, the first feeding chamber evacuation line seconddiameter (D1B) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

In embodiments, the common entry conduit (CEC) ranges in size from:between about 1 inch and about 2 inches; between about 2 inches andabout 3 inches; between about 3 inches and about 4 inches; between about4 inches and about 5 inches; between about 5 inches and about 6 inches;between about 6 inches and about 7 inches; between about 7 inches andabout 8 inches; between about 8 inches and about 9 inches; between about9 inches and about 10 inches; between about 10 inches and about 11inches; between about 11 inches and about 12 inches; between about 12inches and about 13 inches; between about 13 inches and about 14 inches;between about 14 inches and about 15 inches; between about 15 inches andabout 16 inches; between about 16 inches and about 17 inches; betweenabout 17 inches and about 18 inches; between about 18 inches and about19 inches; between about 19 inches and about 20 inches; between about 20inches and about 21 inches; between about 21 inches and about 22 inches;between about 22 inches and about 23 inches; between about 23 inches andabout 24 inches; between about 24 inches and about 25 inches; betweenabout 25 inches and about 26 inches; between about 26 inches and about27 inches; between about 27 inches and about 28 inches; between about 28inches and about 29 inches; between about 29 inches and about 30 inches;between about 30 inches and about 31 inches; between about 31 inches andabout 32 inches; between about 32 inches and about 33 inches; betweenabout 33 inches and about 34 inches; between about 34 inches and about35 inches; between about 35 inches and about 36 inches; between about 36inches and about 37 inches; between about 37 inches and about 38 inches;between about 38 inches and about 39 inches; or, between about 39 inchesand about 40 inches; between about 38 inches and about 39 inches;between about 39 inches and about 40 inches; between about 40 inches andabout 50 inches; between about 50 inches and about 60 inches; betweenabout 60 inches and about 70 inches; between about 70 inches and about80 inches; between about 80 inches and about 90 inches; between about 90inches and about 100 inches; between about 100 inches and about 125inches; between about 125 inches and about 150 inches; or, between about150 inches and about 200 inches.

Second Feeding Chamber (FC2)

The second feeding chamber (FC2) has a second feeding chamber insectevacuation output (205B) or a feeding chamber 2 insect evacuation port(2FC) that is in fluid communication with the insect and gas mixtureinput (303) of the separator (300). A second feeding chamber exitconduit (302B) is connected at one end to the second feeding chamber(FC2) and at another and to a common entry conduit (CEC). The commonentry conduit (CEC) is connected at one end to the second feedingchamber exit conduit (302B) and at another end to the insect and gasmixture input (303) of the separator (300). A feeding chamber 2evacuation valve (VV2) in interposed in the second feeding chamber exitconduit (302B). The feeding chamber 2 evacuation valve (VV2) is equippedwith a with a controller (CV2) that is configured to input and output asignal (XV2) to the computer (COMP). The second feeding chamber exitconduit (302B) has a second feeding chamber evacuation line firstdiameter (D2A) and a second feeding chamber evacuation line reducer(VR2) which merges into a second feeding chamber evacuation line seconddiameter (D2B). In embodiments, the second feeding chamber evacuationline first diameter (D2A) is greater than the second feeding chamberevacuation line second diameter (D2B). In embodiments, the secondfeeding chamber evacuation line first diameter (D2A) is less than thesecond feeding chamber evacuation line second diameter (D2B).

In embodiments, the second feeding chamber evacuation line firstdiameter (D2A) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

In embodiments, the second feeding chamber evacuation line seconddiameter (D2B) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

Third Feeding Chamber (FC3)

The third feeding chamber (FC3) has a third feeding chamber insectevacuation output (205C) or a feeding chamber 3 insect evacuation port(2FC) that is in fluid communication with the insect and gas mixtureinput (303) of the separator (300). The third feeding chamber (FC3) hasa third feeding chamber insect evacuation output (205C) or a feedingchamber 3 insect evacuation port (3FC) that is in fluid communicationwith the insect and gas mixture input (303) of the separator (300). Athird feeding chamber exit conduit (302C) is connected at one end to thethird feeding chamber (FC3) and at another and to a common entry conduit(CEC). The common entry conduit (CEC) is connected at one end to thethird feeding chamber exit conduit (302C) and at another end to theinsect and gas mixture input (303) of the separator (300). A feedingchamber 3 evacuation valve (VV3) in interposed in the third feedingchamber exit conduit (302C). The feeding chamber 3 evacuation valve(VV3) is equipped with a with a controller (CV3) that is configured toinput and output a signal (XV3) to the computer (COMP). The thirdfeeding chamber exit conduit (302C) has a third feeding chamberevacuation line first diameter (D3A) and a third feeding chamberevacuation line reducer (VR3) which merges into a third feeding chamberevacuation line second diameter (D3B). In embodiments, the third feedingchamber evacuation line first diameter (D3A) is greater than the thirdfeeding chamber evacuation line second diameter (D3B). In embodiments,the third feeding chamber evacuation line first diameter (D3A) is lessthan the third feeding chamber evacuation line second diameter (D3B).

In embodiments, the third feeding chamber evacuation line first diameter(D3A) ranges in size from: between about 1 inch and about 2 inches;between about 2 inches and about 3 inches; between about 3 inches andabout 4 inches; between about 4 inches and about 5 inches; between about5 inches and about 6 inches; between about 6 inches and about 7 inches;between about 7 inches and about 8 inches; between about 8 inches andabout 9 inches; between about 9 inches and about 10 inches; betweenabout 10 inches and about 11 inches; between about 11 inches and about12 inches; between about 12 inches and about 13 inches; between about 13inches and about 14 inches; between about 14 inches and about 15 inches;between about 15 inches and about 16 inches; between about 16 inches andabout 17 inches; between about 17 inches and about 18 inches; betweenabout 18 inches and about 19 inches; between about 19 inches and about20 inches; between about 20 inches and about 21 inches; between about 21inches and about 22 inches; between about 22 inches and about 23 inches;between about 23 inches and about 24 inches; between about 24 inches andabout 25 inches; between about 25 inches and about 26 inches; betweenabout 26 inches and about 27 inches; between about 27 inches and about28 inches; between about 28 inches and about 29 inches; between about 29inches and about 30 inches; between about 30 inches and about 31 inches;between about 31 inches and about 32 inches; between about 32 inches andabout 33 inches; between about 33 inches and about 34 inches; betweenabout 34 inches and about 35 inches; between about 35 inches and about36 inches; between about 36 inches and about 37 inches; between about 37inches and about 38 inches; between about 38 inches and about 39 inches;or, between about 39 inches and about 40 inches; between about 38 inchesand about 39 inches; between about 39 inches and about 40 inches;between about 40 inches and about 50 inches; between about 50 inches andabout 60 inches; between about 60 inches and about 70 inches; betweenabout 70 inches and about 80 inches; between about 80 inches and about90 inches; between about 90 inches and about 100 inches; between about100 inches and about 125 inches; between about 125 inches and about 150inches; or, between about 150 inches and about 200 inches.

In embodiments, the third feeding chamber evacuation line seconddiameter (D3B) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

FIG. 15 describes an Insect Production Superstructure System (IPSS) thatinsect feeding module (2000) provides insects contained therein to beable to

Insect Mobility

Large scale insect production systems must be designed responsibly tomake sure that the insects are freed from hunger, thirst, discomfort,pain, injury, disease, fear and distress. Three feeding chambers (FC1,FC2, FC3) are shown in FIG. 15 and the egg-laying insects presenttherein may freely travel from one feeding chamber to another.

The plurality of feeding chambers and a passageways therebetweenencourage egg-laying insects therein to express normal behavior byenabling mobility and relocation to a more suitable living environment.An insect may decide to up and relocate for any reason it chooses or noreason at all. In the event that one breeding chamber lacks sufficientamounts of enhanced feedstock, or is over-crowded, or contains diseasedor cannibalistic insects, the insects may relocate to another feedingchamber to alleviate their discomfort, pain, injury, disease, and fearand distress.

FIG. 15 describes a portion of an Insect Production SuperstructureSystem (IPSS) that permits insects to have mobility and the opportunityto choose between different possible courses of action. Herein aredisclosed advancements and better solutions that meet new requirements,unarticulated needs, or existing market needs in maximizing insectwelfare, maximizing insect output on a minimal physical outlay, andbenefit of large groups of people a high-value animal protein.

The first feeding chamber (FC1) is connected to the second feedingchamber (FC2) via a chamber 2 to chamber 1 transfer line (TL21). Thefirst feeding chamber (FC1) is also connected to the third feedingchamber (FC3) via a chamber 3 to chamber 1 transfer line (TL310). Thefirst feeding chamber (FC1) is also connected to the any one of aplurality of breeding chambers (BC, BC1, BC2. BC3) via a chamber 1breeding chamber transfer line (TLBC1) which is elaborated upon more inFIGS. 16 and 17.

The second feeding chamber (FC2) is connected to the first feedingchamber (FC1) via a chamber 1 to chamber 2 transfer line (TL12). Thesecond feeding chamber (FC2) is also connected to the third feedingchamber (FC3) via a chamber 3 to chamber 2 transfer line (TL32). Thesecond feeding chamber (FC2) is also connected to the any one of aplurality of breeding chambers (BC, BC1, BC2. BC3) via a chamber 2breeding chamber transfer line (TLBC2) which is elaborated upon more inFIGS. 16 and 17.

The third feeding chamber (FC3) is connected to the first feedingchamber (FC1) via a chamber 1 to chamber 3 transfer line (TL13). Thethird feeding chamber (FC3) is also connected to the second feedingchamber (FC2) via a chamber 2 to chamber 3 transfer line (TL23). Thethird feeding chamber (FC3) is also connected to the any one of aplurality of breeding chambers (BC, BC1, BC2. BC3) via a chamber 3breeding chamber transfer line (TLBC3) which is elaborated upon more inFIGS. 16 and 17.

Insect Evacuation

The insect evacuation module (3000) is configured to pull a vacuum oneach one of the plurality of insect feeding chambers at any given timeto evacuate the insects contained therein. A computer (COMP) may beprogrammed to control the operation of the insect evacuation module(3000) to be able to systematically apply a vacuum on any one separateor individually of either of the first feeding chamber (FC1), secondfeeding chamber (FC2), or third feeding chamber (FC3).

The level of the vacuum by the insect evacuation fan (312) may vary.Alternatively, instead of a fan, a vacuum pump, steam jet ejector,pneumatic vacuum, eductor, or any conceivable vacuuming means to realizethe end to pull a vacuum on any number of plurality of feeding chambers(FC1, FC2, FC3) at any given time may be used. At times, it is importantto be able to only draw a vacuum on only one of the feeding chambers atany given time depending upon how far along in the insect growth stageany given feeding chamber (FC1, FC2, FC3) is at. For example, bymeasuring the pressure drop across each of the network of cellscontained within any given feeding chamber (FC1, FC2, FC3), it may bedetermined that it is desirable to only evacuated the insects from say,for example, feeding chamber 1 (FC1) while leaving the other two feedingchambers (FC2, FC3) to remain unchanged to promote stable insect growth.To achieve this end, the computer (COMP) will send a signal (XV1) toonly the feeding chamber 1 evacuation valve (VV1) on the first feedingchamber (FC1) to evacuate the contents therein.

A common insect evacuation pressure sensor (PT10) is installed on thecommon entry conduit (CEC), or alternatively may be installed on anyplurality number of separators (S1, S1, S3). The common insectevacuation pressure sensor (PT10) is configured to input a signal (XT10)to the computer (COMP). A common insect evacuation vent line (VRL) isconnected at one end to the common entry conduit (CEC) and connected atanother end to a header vacuum vent valve (VV0). The header vacuum ventvalve (VV0) is interposed on the common insect evacuation vent line(VRL) and is in fluid communication with both the insect evacuation fan(312) and each one of the plurality of insect feeding chambers (FC1,FC2, FC3). The header vacuum vent valve (VV0) is equipped with acontroller (CV0) that is configured to input and output a signal (XV0)to the computer (COMP). At least one common insect evacuation linereducer (VR0) is interposed on the common insect evacuation vent line(VRL).

The header vacuum vent valve (VV0) is configured to be able to controlthe level of vacuum pulled on a feeding chamber (FC1, FC2, FC3). In theevent that a deep vacuum needs to be pulled to evacuate a feedingchamber that has reached its maximum or desired insect capacity, theheader vacuum vent valve (VV0) may be operatively included in a controlloop while integrated with (i) the common insect evacuation pressuresensor (PT10), and (ii) the controller (316) of the fan motor (314) ofthe insect evacuation fan (312). For example, if a deep vacuum needs tobe pulled on, say feeding chamber 1 (FC1), while leaving the otherfeeding chambers unchanged, the header vacuum vent valve (VV0) mayremain in the closed position to permit the insect evacuation fan (312)to completely draw down the pressure in the feeding chamber 1 (FC1) topull an insect and gas mixture having an insect portion and a gasportion through the first feeding chamber insect evacuation output(205A) and common entry conduit (CEC). If the header vacuum vent valve(VV0) is then opened, or modulated, by any given percentage, it willincrease the gas portion of the insect and gas mixture flowing into theseparator (300) and thus increase the pressure in the feeding chamber(FC1) since not as deep of a vacuum will be pulled on the feedingchamber (FC1). A header vacuum vent valve (VV0) may be able to aide inthe separation of insects and gas within any plurality of separators(S1, S2, S3) contained within the insect evacuation module (3000) byproviding a predictable and consistent inlet velocity at the inlet ofany number of any give plurality of separators (S1, S2, S3).

In embodiments, the egg-laying insects may be evacuated from anyplurality of feeding chambers (FC1, FC2, FC3) by applying a vacuum witha velocity pressure range from: between about 0.001 inches of water toabout 0.002 inches of water; between about 0.002 inches of water toabout 0.003 inches of water; between about 0.003 inches of water toabout 0.006 inches of water; between about 0.006 inches of water toabout 0.012 inches of water; between about 0.012 inches of water toabout 0.024 inches of water; between about 0.024 inches of water toabout 0.050 inches of water; between about 0.050 inches of water toabout 0.075 inches of water; between about 0.075 inches of water toabout 0.150 inches of water; between about 0.150 inches of water toabout 0.300 inches of water; between about 0.300 inches of water toabout 0.450 inches of water; between about 0.450 inches of water toabout 0.473 inches of water; between about 0.473 inches of water toabout 0.496 inches of water; between about 0.496 inches of water toabout 0.521 inches of water; between about 0.521 inches of water toabout 0.547 inches of water; between about 0.547 inches of water toabout 0.574 inches of water; between about 0.574 inches of water toabout 0.603 inches of water; between about 0.603 inches of water toabout 0.633 inches of water; between about 0.633 inches of water toabout 0.665 inches of water; between about 0.665 inches of water toabout 0.698 inches of water; between about 0.698 inches of water toabout 0.733 inches of water; between about 0.733 inches of water toabout 0.770 inches of water; between about 0.770 inches of water toabout 0.808 inches of water; between about 0.808 inches of water toabout 0.849 inches of water; between about 0.849 inches of water toabout 0.891 inches of water; between about 0.891 inches of water toabout 0.936 inches of water; between about 0.936 inches of water toabout 0.982 inches of water; between about 0.982 inches of water toabout 1.031 inches of water; between about 1.031 inches of water toabout 1.083 inches of water; between about 1.083 inches of water toabout 1.137 inches of water; between about 1.137 inches of water toabout 1.194 inches of water; between about 1.194 inches of water toabout 1.254 inches of water; between about 1.254 inches of water toabout 1.316 inches of water; between about 1.316 inches of water toabout 1.382 inches of water; between about 1.382 inches of water toabout 1.451 inches of water; between about 1.451 inches of water toabout 1.524 inches of water; between about 1.524 inches of water toabout 2.286 inches of water; between about 2.286 inches of water toabout 3.429 inches of water; between about 3.429 inches of water toabout 5.143 inches of water; between about 5.143 inches of water toabout 7.715 inches of water; between about 7.715 inches of water toabout 11.572 inches of water; between about 11.572 inches of water toabout 17.358 inches of water; between about 17.358 inches of water toabout 26.037 inches of water; between about 26.037 inches of water toabout 39.055 inches of water; between about 39.055 inches of water toabout 58.582 inches of water; between about 58.582 inches of water toabout 87.873 inches of water; between about 87.873 inches of water toabout 131.810 inches of water; between about 131.810 inches of water toabout 197.715 inches of water; between about 197.715 inches of water toabout 296.573 inches of water; or, between about 296.573 inches of waterto about 400 inches of water.

In embodiments, the egg-laying insects may be evacuated from anyplurality of feeding chambers (FC1, FC2, FC3) by applying a velocityfrom: between about 0.05 feet per second to between about 0.10 feet persecond; 0.10 feet per second to between about 0.15 feet per second; 0.15feet per second to between about 0.25 feet per second; 0.25 feet persecond to between about 0.40 feet per second; 0.40 feet per second tobetween about 0.65 feet per second; 0.65 feet per second to betweenabout 1.05 feet per second; 1.05 feet per second to between about 1.70feet per second; 1.70 feet per second to between about 2.75 feet persecond; 2.75 feet per second to between about 3.09 feet per second; 3.09feet per second to between about 3.64 feet per second; 3.64 feet persecond to between about 4.26 feet per second; 4.26 feet per second tobetween about 4.99 feet per second; 4.99 feet per second to betweenabout 5.84 feet per second; 5.84 feet per second to between about 6.83feet per second; 6.83 feet per second to between about 8.00 feet persecond; 8.00 feet per second to between about 9.37 feet per second; 9.37feet per second to between about 10.97 feet per second; 10.97 feet persecond to between about 12.84 feet per second; 12.84 feet per second tobetween about 15.04 feet per second; 15.04 feet per second to betweenabout 17.61 feet per second; 17.61 feet per second to between about20.61 feet per second; 20.61 feet per second to between about 24.14 feetper second; 24.14 feet per second to between about 28.26 feet persecond; 28.26 feet per second to between about 33.08 feet per second;33.08 feet per second to between about 38.74 feet per second; 38.74 feetper second to between about 45.35 feet per second; 45.35 feet per secondto between about 53.10 feet per second; 53.10 feet per second to betweenabout 62.17 feet per second; 62.17 feet per second to between about72.79 feet per second; 72.79 feet per second to between about 85.23 feetper second; 85.23 feet per second to between about 99.78 feet persecond; 99.78 feet per second to between about 116.83 feet per second;116.83 feet per second to between about 136.79 feet per second; 136.79feet per second to between about 160.15 feet per second; 160.15 feet persecond to between about 187.51 feet per second; 187.51 feet per secondto between about 219.54 feet per second; 219.54 feet per second tobetween about 257.04 feet per second; 257.04 feet per second to betweenabout 300.95 feet per second; 300.95 feet per second to between about352.36 feet per second; 352.36 feet per second to between about 412.55feet per second; 412.55 feet per second to between about 483.02 feet persecond; 483.02 feet per second to between about 565.53 feet per second;565.53 feet per second to between about 662.13 feet per second; 662.13feet per second to between about 775.24 feet per second; 775.24 feet persecond to between about 907.66 feet per second; 907.66 feet per secondto between about 1062.71 feet per second; 1062.71 feet per second tobetween about 1244.24 feet per second; 1244.24 feet per second tobetween about 1456.78 feet per second; or, 1456.78 feet per second tobetween about 1500.00 feet per second.

FIG. 16

FIG. 16 shows a simplistic diagram illustrating a plurality ofseparators (S1, S2, S3) integrated with one common feeding chamber(FC1), and wherein the feeding chamber (FC1) and second separator (S2)are in fluid communication with one common breeding chamber (BC), andwherein the breeding chamber (BC) is in fluid communication with onecommon breeding material and insect separator (SEPIA), and wherein thebreeding material and insect separator (SEPIA) is in fluid communicationwith at least one of a plurality of feeding chambers (FC1, FC2, FC3).

FIG. 16 shows a simplistic diagram illustrating a plurality ofseparators (S1, S2, S3) integrated with one common feeding chamber(FC1), and wherein the feeding chamber (FC1) and second separator (S2)are in fluid communication with one common breeding chamber (BC), andwherein the breeding chamber (BC) is in fluid communication with onecommon breeding material and insect separator (SEPIA), and wherein thebreeding material and insect separator (SEPIA) is in fluid communicationwith at least one of a plurality of feeding chambers (FC1, FC2, FC3).

FIG. 16 shows a portion of the Insect Production Superstructure System(IPSS) including an insect feeding module (2000), an insect evacuationmodule (3000), an insect breeding module (4000), and hatched insectseparation module (5000). The insect feeding module (2000) is configuredto feed the enhanced feedstock from the enhanced feedstock mixing module(1000) and grow insects so that egg-laying insects may in turn lay eggs.The insect evacuation module (3000) is configured to remove insects,residual enhanced feedstock, particulates including insect exoskeletonfrom the any of a plurality of insect feeding modules (2000, 2000A,200B, 2000C). The insect breeding module (4000) is configured to removeeggs from the insect feeding module (2000) for incubation over atemperature and humidity controlled duration of time to formhatched-insects. The hatched insect separation module (5000) isconfigured to separate the hatched-insects and breeding material fromthe insect breeding module (4000) and then distribute the separatedbreeding material to any one of the plurality of the insect feedingmodules (2000, 2000A, 2000B, 2000C)

FIG. 16 shows an insect feeding module (2000) including one feedingchamber (FC1) integrated with an insect evacuation module (3000)comprised of a first separator (S1), second separator (S2), and a thirdseparator (S3). FIG. 16 shows the first separator (S1) and secondseparator (S2) as cyclones. FIG. 16 also shows the third separator (S3)as a filter. It is to be noted that the embodiment of FIG. 16 isnon-limiting and shall not be construed to limit the disclosure in anyway. Any number of separators (S1, S2, S3) may be employed and anypermutation or combination of separation unit operations or devices maybe used so long as insect portion (304A) is separated from a gas portion(304B) of an insect and gas mixture (304).

FIG. 16 shows the first separator (S1) as a first insect coarseseparator (S1A), the second separator (S2) as a second insect fineseparator (S2A), and the third separator (S3) as a particulate separator(S3A). The first insect coarse separator (S1A) is configured to remove aportion of the insect portion (304A) separated from the gas portion(304B) of an insect and gas mixture (304). The second insect fineseparator (S2A) is configured to remove insects smaller than the insectsseparated in the first insect coarse separator (S1A). The particulateseparator (S3A) is configured to remove particulates such as remnants ofenhanced feedstock, or fine polymer particulate, for example, not onlyincluding pieces of portions of insect exoskeleton. The particulateseparator (S3A) is in fluid communication with the polymer distributionmodule (1D) and is configured to transfer a portion of the separatedparticulate to the polymer tank (1D2) as polymer (1D1).

First Separator (S1), First Insect Coarse Separator (S1A)

The first insect coarse separator (S1A) has a first insect coarseseparator input (S1A1) that is in fluid communication with the firstfeeding chamber insect evacuation output (205A) of the first feedingchamber (FC1) via a first feeding chamber exit conduit (302A). The firstinsect coarse separator (S1A) is configured to accept an insect and gasmixture (304) from the first feeding chamber (FC1), separate a portionof the insects from the gas and output a first insect-depleted gasstream (355) via a coarse separator gas and insect mixture output (356).

The first separator (S1) is equipped with a first dipleg (357), a firstseparator conveyor (358), and a first separator valve (361) interposedon the first dipleg (357). A first separated insect stream (360) isrouted down the first dipleg (357), through the first separator valve(361) and into the first separator conveyor (358). In embodiments, thefirst separator conveyor (358) is a compression screw (359) which servesto instantly kill insects by compressing them. The first separatedinsect stream (360) may in turn be sent to a grinder (1250) within aninsect grinding module via a first separated insect stream input (371).In other embodiments, the first separated insect stream (360) may besent to a pathogen removal unit (1550) within a pathogen removal module,or to a within a lipid extraction unit (1501) lipid extraction module.

Second Separator (S2), Second Insect Fine Separator (S2A)

The second insect fine separator (S2A) has a second insect fineseparator input (S2A1) that is in fluid communication with the coarseseparator gas and insect mixture output (356) of the first insect coarseseparator (S1A). The second insect fine separator (S2A) is configured toaccept a first insect-depleted gas stream (355) from the first insectcoarse separator (S1A), separate a portion of the insects from the gasand output a second insect-depleted gas stream (362) via a fineseparator gas and particulate mixture output (363).

The second separator (S2) is equipped with a second dipleg (364), asecond separator conveyor (365), and a second separator valve (368)interposed on the second dipleg (364). A second separated insect stream(360) is routed down the second dipleg (364), through the secondseparator valve (368) and into the second separator conveyor (365). Inembodiments, the second separator conveyor (365) is a compression screw(366) which serves to instantly kill insects by compressing them.

In embodiments, the second separator conveyor (365) is a not acompression screw (366) but instead routes the second separated insectstream (367) to the to a breeding chamber (BC) via a breeding chamberfine separated insect portion input (375). In embodiments, the secondseparator conveyor (365) is a not a compression screw (366) but insteadroutes the second separated insect stream (367) to a plurality of otherdestinations such as to the grinder (1250), pathogen removal unit(1550), or lipid extraction unit (1501). The second separated insectstream (367) may be sent to a grinder (1250) within an insect grindingmodule via a first separated insect stream input (371). In otherembodiments, the second separated insect stream (367) may be sent to apathogen removal unit (1550) within a pathogen removal module, or to awithin a lipid extraction unit (1501) lipid extraction module.

Third Separator (S3), Particulate Separator (S3A)

The particulate separator (S3A) has a particulate separator input (S3A1)that is in fluid communication with the fine separator gas andparticulate mixture output (363) of the second insect fine separator(S2A). The particulate separator (S3A) is configured to accept a secondinsect-depleted gas stream (362) from the second insect fine separator(S2A), separate a portion of the particulates from the gas and output aparticulate-depleted gas stream (369) to the insect evacuation fan(312).

The insect evacuation fan (312) is in fluid with the breeding chamber(BC) via a breeding chamber exhaust input (376) and is configured todischarge the exhaust (377) into the breeding chamber (BC). Inembodiments, the separated insect conveyor (328) of the third separator(S3) particulate separator (S3A) is in fluid communication with thepolymer distribution module (1D) and is configured to transfer a portionof the separated particulate stream (370) to the polymer tank (1D2) aspolymer (1D1).

Insect Breeding Module (4000)

FIG. 16 shows the insect feeding module (2000) integrated with theinsect breeding module (4000). The insect breeding module (4000) isconfigured to remove eggs from the insect feeding module (2000) forincubation over a temperature and humidity controlled duration of timeto form hatched-insects.

The insect breeding module (4000) contains a breeding chamber (BC). FIG.16 shows one breeding chamber (BC) portrayed as breeding chamber 1(BC1). It is to be noted that FIG. 16 shows a first feeding chamber(FC1) connected to a breeding chamber 1 (BC1) via a feeding chamber 1egg-laden breeding material transfer line (R1).

The feeding chamber 1 egg-laden breeding material transfer line (R1) isconnected at one end to the first feeding chamber (FC1) via a conveyoroutput (249) and at another end to breeding chamber 1 (BC1) via afeeding chamber 1 breeding chamber 1 input (BC1A). The feeding chamber 1egg-laden breeding material transfer line (R1) is configured to transferan egg-laden breeding material (250) to the interior (BCIN) of breedingchamber 1 (BC1). In embodiments, the interior (BCIN) of the breedingchamber 1 (BC1) contains a tiered plurality of conveyors that include atleast an upper and a lower conveyor wherein egg-laden breeding material(250) is transferred from conveyors spaced apart from one another in avertical orientation to permit sufficient time to incubate the eggscontained within the egg-laden breeding material (250) to hatch insects.

FIG. 16 shows egg-laden breeding material (250) being transferred to theinterior (BCIN) of the breeding chamber 1 (BC1) where it is firstelevated via a first conveyor transfer unit (XY1A) to the first conveyorheight (CH1A) of a first conveyor (CY1A) operating in a clockwise motionof operation.

The first conveyor (CY1A) is positioned at a vertical height above atleast one other conveyor. FIG. 16 shows seven conveyors (CY1A, CY2A,CY3A, CY4A, CY5A, CY6A, CY7A) and the first conveyor (CY1A) ispositioned at a vertical height above each one of a second conveyor(CY2A), third conveyor (CY3A), fourth conveyor (CY4A), fifth conveyor(CY5A), sixth conveyor (CY6A), and seventh conveyor (CY7A). The secondconveyor (CY2A) is positioned at a vertical height above each one of athird conveyor (CY3A), fourth conveyor (CY4A), fifth conveyor (CY5A),sixth conveyor (CY6A), and seventh conveyor (CY7A). The third conveyor(CY3A) is positioned at a vertical height above each one of a fourthconveyor (CY4A), fifth conveyor (CY5A), sixth conveyor (CY6A), andseventh conveyor (CY7A). The fourth conveyor (CY4A) is positioned at avertical height above each one of a fifth conveyor (CY5A), sixthconveyor (CY6A), and seventh conveyor (CY7A). The fifth conveyor (CY5A)is positioned at a vertical height above each one of a sixth conveyor(CY6A), and seventh conveyor (CY7A). The sixth conveyor (CY6A) ispositioned at a vertical height above the seventh conveyor (CY7A).

The first conveyor (CY1A) is installed at a first conveyor height (CH1A)above the second conveyor (CY2A). The second conveyor (CY2A) isinstalled at a second conveyor height (CH2A) above the third conveyor(CY3A). The third conveyor (CY3A) is installed at a third conveyorheight (CH3A) above the fourth conveyor (CY4A). The fourth conveyor(CY4A) is installed at a fourth conveyor height (CH4A) above the fifthconveyor (CY5A). The fifth conveyor (CY5A) is installed at a fifthconveyor height (CH5A) above the sixth conveyor (CY6A). The sixthconveyor (CY6A) is installed at a sixth conveyor height (CH6A) above theseventh conveyor (CY7A).

The seventh conveyor (CY7A) is installed at a seventh conveyor height(CH7A) below all other conveyors (CY1A, CY2A, CY3A, CY4A, CY5A, CY6A).FIG. 16 shows the first conveyor (CY1A), third conveyor (CY3A), fifthconveyor (CY5A), seventh conveyor (CY7A) all configured to operate in aclockwise motion of operation. FIG. 16 shows the second conveyor (CY2A),fourth conveyor (CY4A), sixth conveyor (CY6A), all configured to operatein a counter-clockwise motion of operation.

A conveyor 1 to conveyor 2 transfer unit (XY2A) is configured totransfer the egg-laden breeding material from the first conveyor (CY1A)to the second conveyor (CY2A). The conveyor 2 to conveyor 3 transferunit (XY3A) is configured to transfer the egg-laden breeding materialfrom the second conveyor (CY2A) to the third conveyor (CY3A). Theconveyor 3 to conveyor 4 transfer unit (XY4A) is configured to transferthe egg-laden breeding material from the third conveyor (CY3A) to thefourth conveyor (CY4A). The conveyor 4 to conveyor 5 transfer unit(XY5A) is configured to transfer the egg-laden breeding material fromthe fourth conveyor (CY4A) to the fifth conveyor (CY5A). The conveyor 5to conveyor 6 transfer unit (XY6A) is configured to transfer theegg-laden breeding material, and perhaps hatched insects, from the fifthconveyor (CY5A) to the sixth conveyor (CY6A). The conveyor 6 to conveyor7 transfer unit (XY7A) is configured to transfer the egg-laden breedingmaterial, and perhaps hatched insects, from the sixth conveyor (CY6A) tothe seventh conveyor (CY7A). The seventh conveyor (CY7A) is configuredto transfer the hatched insects and breeding material from the feedingchamber 1 breeding chamber output (BC1B) of the interior (BCIN) of thebreeding chamber (BC) to the interior (SIN1) of the breeding materialand insect separator (SEPIA) contained within the hatched insectseparation module (5000).

Hatched Insect Separation Module (5000)

FIG. 16 shows the hatched insect separation module (5000) equipped witha breeding material and insect separator (SEPIA) and a breeding materialtank (500). The breeding material and insect separator (SEPIA) includesan interior (SIN1), a separator input (1SEPA), a separator materialoutput (1SEPB), and a separator insect output (1SEPC). The breedingmaterial and insect separator (SEPIA) is connected to breeding chamber 1(BC1) via a breeding chamber 1 hatched egg and breeding materialtransfer line (U1). The breeding chamber 1 hatched egg and breedingmaterial transfer line (U1) is connected at one end to the breedingchamber 1 (BC1) via a feeding chamber 1 breeding chamber output (BC1B)and connected at another end to the breeding material and insectseparator (SEPIA) via a separator input (1SEPA).

The separator input (1SEPA) is configured to accept hatched insects andbreeding material from the seventh conveyor (CY7A) of breeding chamber 1(BC1), and separate hatched insects (400) from the breeding material(523). The separator insect output (1SEPC) is configured to dischargehatched insects (400) from the interior (SIN1) of the breeding materialand insect separator (SEPIA) and route the hatched insects (400) toeither one of a plurality of feeding chambers (FC1, FC2, FC3) via aseparator hatched insect transfer line (01). Specifically, separatorinsect output (1SEPC) is configured to discharge hatched insects (400)first feeding chamber (FC1) via a separator feeding chamber 1 transferline (011), or to the second feeding chamber (FC2) via a separatorfeeding chamber 2 transfer line (012), or to the third feeding chamber(FC3) via a separator feeding chamber 3 transfer line (013). Hatchedinsects (400) transferred from the hatched insect separation module(5000) to the insect feeding module (2000) are made available to thefirst feeding chamber (FC1) via a separator feeding chamber 1 transferline (011) and a chamber 1 breeding chamber transfer line (TLBC1).

Breeding material (523) separated from the hatched insects (400) withinthe interior (SIN1) of the breeding material and insect separator(SEPIA) is routed to the interior (501) of a breeding material tank(500) via a separator material output (1SEPB). The breeding material(523) separated from the hatched insects (400) within the interior(SIN1) of the breeding material and insect separator (SEPIA) may becharacterized as an egg-depleted material (518) since eggs wereincubated to form hatched insects (400). A material transfer line (522)is connected at one end to the separator material output (1SEPB) of thebreeding material and insect separator (SEPIA) and connected at anotherend to the breeding material input (502) of the breeding material tank(500). An egg-depleted material transfer conveyor (519) may beinterposed in the material transfer line (522) in between the breedingmaterial and insect separator (SEPIA) and the breeding material tank(500).

The breeding material tank (500) has an interior (501), a breedingmaterial input (502), and a breeding material output (510). The breedingmaterial tank (500) also has a top section (503), a bottom section(506), and an interior (501) defined by at least one side wall (507). Abreeding material screw conveyor (508) is located at the bottom section(506) and configured to transfer breeding material to either one of aplurality of feeding chambers (FC1, FC2, FC3) via a breeding materialtransfer line (511). The breeding material transfer line (511) isconnected at one end to any one of a plurality of feeding chambers (FC1,FC2, FC3) and connected at another end to the breeding material screwconveyor (508) via a breeding material output (510). The breedingmaterial screw conveyor (508) is equipped with a breeding material screwconveyor motor (512), controller (513), and is configured to input andoutput a signal (514) to the computer (COMP).

FIG. 17

FIG. 17 shows a perspective view of one embodiment of a scalableportable modular Insect Production Superstructure System (IPSS) designedwith: one enhanced feedstock mixing module (1000); three insect feedingmodules (2000A, 2000B, 2000C); one insect evacuation module (3000);three insect breeding modules (4000A, 4000B, 4000C), and three insectseparation modules (5000).

FIG. 17 shows a perspective view of one embodiment of a scalableportable modular Insect Production Superstructure System (IPSS) designedwith: one enhanced feedstock mixing module (1000); three insect feedingmodules (2000A, 2000B, 2000C); one insect evacuation module (3000);three insect breeding modules (4000A, 4000B, 4000C), and three insectseparation modules (5000).

In one embodiment, each module (1000, 2000A, 2000B, 2000C, 3000, 4000A,4000B, 4000C, 5000) container is a 40 feet high cube containerconforming to the International Organization for Standardization (ISO)specifications. In another embodiment, the container may measure 40feet×8 feet×9.6 feet. In another embodiment, other containers ofdifferent sizes may be used.

In embodiments, each module (1000, 2000A, 2000B, 2000C, 3000, 4000A,4000B, 4000C, 5000) may be positioned on high density plastic ties(HDT). The high density plastic ties (HDT) provide stability to themodule (1000, 2000A, 2000B, 2000C, 3000, 4000A, 4000B, 4000C, 5000) ofthe Insect Production Superstructure System (IPSS) and may be cheaperand faster to install than traditional concrete foundations. In anotherembodiment, each of the module (1000, 2000A, 2000B, 2000C, 3000, 4000A,4000B, 4000C, 5000) may be positioned on concrete foundations.Electrical cables may be contained in a plurality of fiberglass cabletrays (FGT) placed between each module (1000, 2000A, 2000B, 2000C, 3000,4000A, 4000B, 4000C, 5000).

The embodiment of FIG. 17 shows the enhanced feedstock mixing module(1000) including a feedstock distribution module (1A), mineraldistribution module (1B), vitamin distribution module (1C), polymerdistribution module (1D), water distribution module (1E), and enhancedfeedstock distribution module (1F),

However, as depicted in FIGS. 18-20 the water distribution module (1E)and enhanced feedstock distribution module (1F) may be separate from theenhanced feedstock mixing module (1000). A separate water distributionmodule (1E) and a separate enhanced feedstock distribution module (1F)are not shown in FIG. 17 because it these modules (1E, 1F) are designedto be housed within the enhanced feedstock mixing module (1000). Aseparate water distribution module (1E) is shown in FIGS. 21-23. Aseparate and a separate enhanced feedstock distribution module (1F) isshown in FIGS. 24-26.

In the non-limiting example of FIG. 17 for a variable-scale, modular,easily manufacturable, energy efficient, reliable, and computer operatedInsect Production Superstructure Systems (IPSS) shows one enhancedfeedstock mixing module (1000) in fluid communication with a firstinsect feeding module (2000A), second insect feeding module (2000B), anda third insect feeding module (2000C).

A first enhanced feedstock stream (EF1) is configured to pass from theenhanced feedstock mixing module (1000) to the first insect feedingmodule (2000A). A second enhanced feedstock stream (EF2) is configuredto pass from the enhanced feedstock mixing module (1000) to the secondinsect feeding module (2000B). A third enhanced feedstock stream (EF3)is configured to pass from the enhanced feedstock mixing module (1000)to the third insect feeding module (2000C).

Each of the first insect feeding module (2000A), second insect feedingmodule (2000B), third insect feeding module (2000C), are connected toone common insect evacuation module (3000) via a common entry conduit(CEC). The common entry conduit (CEC) is connected at one end to theinsect evacuation module (3000) and connected at one end to the firstinsect feeding module (2000A) via a first feeding chamber insectevacuation output (205A). The common entry conduit (CEC) is connected atone end to the insect evacuation module (3000) and connected at one endto the second insect feeding module (2000B) via a second feeding chamberinsect evacuation output (205B). The common entry conduit (CEC) isconnected at one end to the insect evacuation module (3000) andconnected at one end to the third insect feeding module (2000C) via athird feeding chamber insect evacuation output (205C). Each insectfeeding module (2000A, 2000B, 2000C) is connected to its own insectbreeding module (4000A, 4000B, 4000C). The first insect feeding module(2000A) is connected to the first insect breeding module (4000A) via afeeding chamber 1 egg-laden breeding material transfer line (R1). Thesecond insect feeding module (2000B) is connected to the second insectbreeding module (4000B) via a feeding chamber 2 egg-laden breedingmaterial transfer line (R2). The third insect feeding module (2000C) isconnected to the third insect breeding module (4000C) via a feedingchamber 3 egg-laden breeding material transfer line (R3).

Each insect breeding module (4000A, 4000B, 4000C) is connected to itsown hatched insect separation module (5000A, 5000B, 5000C). The firstinsect breeding module (4000A) is connected to the first hatched insectseparation module (5000A) via a breeding chamber 1 hatched egg andbreeding material transfer line (U1). The second insect breeding module(4000B) is connected to the second hatched insect separation module(5000B) via a breeding chamber 2 hatched egg and breeding materialtransfer line (U2). The third insect breeding module (4000C) isconnected to the third hatched insect separation module (5000C) via abreeding chamber 3 hatched egg and breeding material transfer line (U3).

Each hatched insect separation module (5000A, 5000B, 5000C) is connectedto any of the plurality of insect feeding modules (2000A, 2000B, 2000C)via a first hatched insect output (DFC), second hatched insect output(EFC), and third hatched insect output (FFC). The first hatched insectoutput (DFC) of the first hatched insect separation module (5000A) is influid communication with the first insect feeding module (2000A) via afirst hatched insect input (AFC). The first hatched insect output (DFC)of the first hatched insect separation module (5000A) is in fluidcommunication with the second insect feeding module (2000B) via a secondhatched insect input (BFC). The first hatched insect output (DFC) of thefirst hatched insect separation module (5000A) is in fluid communicationwith the third insect feeding module (2000C) via a third hatched insectinput (CFC).

The second hatched insect output (EFC) of the second hatched insectseparation module (5000B) is in fluid communication with the firstinsect feeding module (2000A) via a first hatched insect input (AFC).The second hatched insect output (EFC) of the second hatched insectseparation module (5000B) is in fluid communication with the secondinsect feeding module (2000B) via a second hatched insect input (BFC).The second hatched insect output (EFC) of the second hatched insectseparation module (5000B) is in fluid communication with the thirdinsect feeding module (2000C) via a third hatched insect input (CFC).

The third hatched insect output (FFC) of the third hatched insectseparation module (5000C) is in fluid communication with the firstinsect feeding module (2000A) via a first hatched insect input (AFC).The third hatched insect output (FFC) of the third hatched insectseparation module (5000C) is in fluid communication with the secondinsect feeding module (2000B) via a second hatched insect input (BFC).The third hatched insect output (FFC) of the third hatched insectseparation module (5000C) is in fluid communication with the thirdinsect feeding module (2000C) via a third hatched insect input (CFC).

FIG. 18

FIG. 18 shows a front view of one embodiment of an enhanced feedstockmixing module (1000) module including a feedstock distribution module(1A), mineral distribution module (1B), vitamin distribution module(1C), and a polymer distribution module (1D). The enhanced feedstockmixing module (1000) is shown to be contained within a 40 feet high cubecontainer conforming to the International Organization forStandardization (ISO) specifications.

The feedstock distribution module (1A) has feedstock (1A1) containedwithin the interior (1A3) of a feedstock tank (1A2). A feedstock masssensor (1A7) is provided to determine the loss in mass of the feedstocktank (1A2). The feedstock tank (1A2) has a live floor screw (1A21) witha motor (1A22) is configured to transfer feedstock (1A1) from theinterior (1A3) of the feedstock tank (1A2) to a feedstock conveyor (1A5)and an enhanced feedstock transport screw (1A20). A supply access door(1A15) is positioned above the feedstock input (1A4) and configured totransfer feedstock (1A1) to the interior (1A3) of the feedstock tank(1A2). A supply access door opening/closing unit (1A16) is operativelycoupled to the supply access door (1A15) and a weather seal (1A17) is incontact with the supply access door (1A15) to prevent rain and otherelements from entering the enhanced feedstock mixing module (1000).

The mineral distribution module (1B) has minerals (1B1) contained withinthe interior (1B3) of a mineral tank (1B2). A mineral mass sensor (1B7)is provided to determine the loss in mass of the mineral tank (1B2). Themineral tank (1B2) has a live floor screw (1B20) with a motor (1B21) isconfigured to transfer minerals (1B1) from the interior (1B3) of themineral tank (1B2) to a mineral conveyor (1B5) and an enhanced feedstocktransport screw (1A20) via an enhanced feedstock transport screwconnection (1B18). A supply access door (1B13) is positioned above themineral input (1B4) and configured to transfer minerals (1B1) to theinterior (1B3) of the mineral tank (1B2). A supply access dooropening/closing unit (1B14) is operatively coupled to the supply accessdoor (1B13) and a weather seal (1B1S) is in contact with the supplyaccess door (1B13) to prevent rain and other elements from entering theenhanced feedstock mixing module (1000).

The vitamin distribution module (1C) has vitamins (1C1) contained withinthe interior (1C3) of a vitamin tank (1C2). A vitamin mass sensor (1C7)is provided to determine the loss in mass of the vitamin tank (1C2). Thevitamin tank (1C2) has a live floor screw (1C20) with a motor (1C21) isconfigured to transfer vitamins (1C1) from the interior (1C3) of thevitamin tank (1C2) to a vitamin conveyor (105) and an enhanced feedstocktransport screw (1A20) via an enhanced feedstock transport screwconnection (1C18). A supply access door (1C13) is positioned above thevitamin input (1C4) and configured to transfer vitamins (1C1) to theinterior (1C3) of the vitamin tank (1C2). A supply access dooropening/closing unit (1C14) is operatively coupled to the supply accessdoor (1C13) and a weather seal (1C15) is in contact with the supplyaccess door (1C13) to prevent rain and other elements from entering theenhanced feedstock mixing module (1000).

The polymer distribution module (1D). includes polymer (1D1) containedwithin the interior (1D3) of a polymer tank (1D2). A polymer mass sensor(1D7) is provided to determine the loss in mass of the polymer tank(1D2). The polymer tank (1D2) has a live floor screw (1D20) with a motor(1D21) is configured to transfer polymer (1D1) from the interior (1D3)of the polymer tank (1D2) to a polymer conveyor (1D5) and an enhancedfeedstock transport screw (1A20) via an enhanced feedstock transportscrew connection (1D18). A supply access door (1D13) is positioned abovethe polymer input (1D4) and configured to transfer polymer (1D1) to theinterior (1D3) of the polymer tank (1D2). A supply access dooropening/closing unit (1C14) is operatively coupled to the supply accessdoor (1C13) and a weather seal (1C15) is in contact with the supplyaccess door (1C13) to prevent rain and other elements from entering theenhanced feedstock mixing module (1000).

A dry enhanced feedstock (DEF) is outputted from the enhanced feedstockmixing module (1000) via the enhanced feedstock transport screw (1A20).A feedstock moisture sensor (1A12A) is interposed on the enhancedfeedstock transport screw (1A20) to measure the water content of the dryenhanced feedstock (DEF). Alternately, the feedstock moisture sensor(1A12A) may be positioned on the enhanced feedstock transport screw(1A20) after the minerals (1B1), vitamins (1C1), polymer (1D1) have beenmixed with the feedstock (1A1). The enhanced feedstock mixing module(1000) may be equipped with a low voltage disconnect switch (1000LV) anda computer (COMP).

FIG. 19

FIG. 19 shows a top view of one embodiment of an enhanced feedstockmixing module (1000) including a feedstock distribution module (1A),mineral distribution module (1B), vitamin distribution module (1C), anda polymer distribution module (1D).

Feedstock (1A1) within the feedstock tank (1A2), minerals (1B1) withinthe mineral tank (1B2), vitamins (1C1) within the vitamin tank (1C2),and polymer (1D1) within the polymer tank (1D2) are all mixed togetherin an enhanced feedstock transport screw (1A20). A live floor screw(1A21) equipped with a motor (1A22) is positioned within the feedstocktank (1A2). The live floor screw (1A21) transfers feedstock (1A1) to afeedstock conveyor (1A5). The feedstock conveyor (1A5) has a feedstockconveyor output (1A6) that is connected to a feedstock transfer line(1A14). The feedstock transfer line (1A14) is connected at one end tothe feedstock conveyor output (1A6) and at another end to the enhancedfeedstock transport screw (1A20) via an enhanced feedstock transportscrew connection (1A20A). The feedstock distribution module (1A) isequipped with an air inlet vent (1A18) that is configured to input air(1A19) to the feedstock distribution module (1A) portion of the enhancedfeedstock mixing module (1000). A feedstock module access door (1A23) isprovided to access the feedstock distribution module (1A) portion of theenhanced feedstock mixing module (1000).

A live floor screw (1B20) equipped with a motor (1B21) is positionedwithin the mineral tank (1B2). The live floor screw (1B20) transfersminerals (1B1) to a mineral conveyor (1B5). The mineral conveyor (1B5)has a mineral conveyor output (1B6) that is connected to a mineraltransfer line (1B12). The mineral transfer line (1B12) is connected atone end to the mineral conveyor output (1B6) and at another end to theenhanced feedstock transport screw (1A20) via an enhanced feedstocktransport screw connection (1B18). The mineral distribution module (1B)is equipped with an air inlet vent (1B16) that is configured to inputair (1B17) to the mineral distribution module (1B) portion of theenhanced feedstock mixing module (1000). A mineral module access door(1B22) is provided to access the mineral distribution module (1B)portion of the enhanced feedstock mixing module (1000).

A live floor screw (1C20) equipped with a motor (1C21) is positionedwithin the vitamin tank (1D2). The live floor screw (1C20) transfersvitamins (1C1) to a vitamin conveyor (105). The vitamin conveyor (105)has a vitamin conveyor output (106) that is connected to a vitamintransfer line (1C12). The vitamin transfer line (1C12) is connected atone end to the vitamin conveyor output (106) and at another end to theenhanced feedstock transport screw (1A20) via an enhanced feedstocktransport screw connection (1C18). The vitamin distribution module (1C)is equipped with an air inlet vent (1C16) that is configured to inputair (1C17) to the vitamin distribution module (1C) portion of theenhanced feedstock mixing module (1000). A vitamin module access door(1C22) is provided to access the vitamin distribution module (1C)portion of the enhanced feedstock mixing module (1000).

A live floor screw (1D20) equipped with a motor (1D21) is positionedwithin the polymer tank (1D2) to transfer polymer (1D1) to a polymerconveyor (1D5). The polymer conveyor (1D5) has a polymer conveyor output(1D6) that is connected to a polymer transfer line (1D12). The polymertransfer line (1D12) is connected at one end to the polymer conveyoroutput (1D6) and at another end to the enhanced feedstock transportscrew (1A20) via an enhanced feedstock transport screw connection(1D18). The polymer distribution module (1D) is equipped with an airinlet vent (1D16) that is configured to input air (1D17) to the polymerdistribution module (1D) portion of the enhanced feedstock mixing module(1000). A polymer module access door (1D22) is provided to access thepolymer distribution module (1D) portion of the enhanced feedstockmixing module (1000). The polymer distribution module (1D) is in fluidcommunication with the third separator (S3) particulate separator (S3A)of the insect evacuation module (3000). The polymer tank (1D2) isconfigured to accept a polymer (1D1) from a portion of the separatedparticulate stream (370) of the separated insect conveyor (328) of thethird separator (S3) particulate separator (S3A).

FIG. 20

FIG. 20 shows a first side view of one embodiment of an enhancedfeedstock mixing module (1000). Visible from the first side view of theenhanced feedstock mixing module (1000) is the supply access door (1A15)that is opened and closed by a supply access door opening/closing unit(1A16) wherein a weather seal (1A17) prevents rain and other elementsfrom entering the enhanced feedstock mixing module (1000).

Feedstock (1A1) is contained within the interior (1A3) of the feedstocktank (1A2). Feedstock (1A1) is added to the enhanced feedstock mixingmodule (1000) through the supply access door (1A15) where it enters thefeedstock input (1A4) and into the interior (1A3) of the feedstock tank(1A2). A live floor screw (1A21) is positioned in the interior (1A3) ofthe feedstock tank (1A2). The live floor screw (1A21) is configured totransfer feedstock (1A1) from the interior (1A3) of the feedstock tank(1A2) into a feedstock conveyor (1A5). The feedstock conveyor motor(1A9) drives the feedstock conveyor (1A5) to transport feedstock (1A1)through the feedstock conveyor output (1A6) and into the enhancedfeedstock transport screw (1A20) via an enhanced feedstock transportscrew connection (1A20A). A feedstock mass sensor (1A7) may bepositioned on the feedstock conveyor (1A5) to measure the mass loss andcontrol to a pre-determined feedstock mass flow rate into the enhancedfeedstock transport screw (1A20). Also visible is the feedstock moduleaccess door (1A23) and an air inlet vent (1A18) which permits air (1A19)to enter the feedstock distribution module (1A) portion of the enhancedfeedstock mixing module (1000).

FIG. 21

FIG. 21 shows a front view of one embodiment of a water distributionmodule (1E). The following description for FIG. 21 also applies to FIG.22 since the reference numerals for FIG. 20 and FIG. 21 are identical.The water distribution module (1E) is shown to be contained within a 40feet high cube container conforming to the International Organizationfor Standardization (ISO) specifications.

The water distribution module (1E) contains a first water treatment unit(1E6), second water treatment unit (1E11), water distribution module(1E) enhancer tank (1E45) and a water supply pump (1E22). A water inputline (1E4) enters the water distribution module (1E) and is connected tothe first water treatment unit (1E6) at a first water treatment unitinput (1E7). A first water pressure sensor (1E2) is installed on thewater input line (1E4). The first water treatment unit (1E6) may containa contain an adsorbent, ion-exchange resin, catalyst, or activatedcarbon.

The first water treatment unit (1E6) is connected to the second watertreatment unit (1E11) via a first contaminant-depleted water transferline (1E10). The first contaminant-depleted water transfer line (1E10)is connected at one end to the first water treatment unit output (1E8)of the first water treatment unit (1E6) and connected at a second end tothe second water treatment unit input (1E12) of the second watertreatment unit (1E11). The second water treatment unit (1E11) maycontain a contain an adsorbent, ion-exchange resin, catalyst, oractivated carbon. The system as shown in FIGS. 21-23 may, for example beused to decontaminate water that contains positively charged ions andnegatively charged ions and optionally undesirable compounds. Thepositively charged ions are comprised of one or more from the groupconsisting of calcium, magnesium, sodium, and iron. The negativelycharged ions are comprised of one or more from the group consisting ofiodine, chloride, and sulfate. The undesirable compounds are comprisedof one or more from the group consisting of dissolved organic chemicals,viruses, bacteria, and particulates. In embodiments, the first watertreatment unit (1E6) contains activated carbon and the second watertreatment unit (1E11) contains a molecular sieve adsorbent.

In embodiments, the first water treatment unit (1E6) includes a cationconfigured to remove positively charged ions from water to form apositively charged ion depleted water, the positively charged ions arecomprised of one or more from the group consisting of calcium,magnesium, sodium, and iron. In embodiments, the second water treatmentunit (1E11) includes an anion configured to remove negatively chargedions from the positively charged ion depleted water to form a negativelycharged ion depleted water, the negatively charged ions are comprised ofone or more from the group consisting of iodine, chloride, and sulfate.In embodiments, the first water treatment unit (1E6) includes a cationand an anion. In embodiments, the second water treatment unit (1E11)includes a membrane configured to remove undesirable compounds from thenegatively charged ion depleted water to form some undesirable compoundsdepleted water, the undesirable compounds are comprised of one or morefrom the group consisting of dissolved organic chemicals, viruses,bacteria, and particulates. In embodiments, the second water treatmentunit (1E11) includes a membrane configured to remove undesirablecompounds from the water to form some undesirable compounds depletedwater, the undesirable compounds are comprised of one or more from thegroup consisting of dissolved organic chemicals, viruses, bacteria, andparticulates.

The second water treatment unit (1E11) is connected to the water tank(1E16) via a second contaminant-depleted water transfer line (1E15). Thesecond contaminant-depleted water transfer line (1E15) is connected atone end to the second water treatment unit output (1E13) of the secondwater treatment unit (1E11) and connected at another end to the waterinput (1E18) of the water tank (1E16). A water supply valve (1E23) witha controller (1E24) is interposed on the second contaminant-depletedwater transfer line (1E15) in between the second water treatment unit(1E11) and water tank (1E16). The water tank (1E16) has an interior(1E17) that contains water (1E1). The water tank (1E16) is equipped witha high water level sensor (1E26) and a low water level sensor (1E28).

Enhancers (1E44) contained within the interior (1E46) of the enhancertank (1E45) may be routed to the interior (1E17) of the water tank(1E16) through an enhancer transfer line (1E48). The enhancer transferline (1E48) is connected at one end to the enhancer tank output (1E47)of the enhancer tank (1E45) and connected at another end to the enhancerinput (1E49) of the water tank (1E16). A water enhancer supply valve(1E52) with a controller (1E53) is interposed on the enhancer transferline (1E48) in between the enhancer tank (1E45) and the water tank(1E16). An enhancer flow sensor (1E50) is interposed on the enhancertransfer line (1E48) in between the enhancer tank (1E45) and the watertank (1E16).

A water supply pump (1E22) is connected to the water tank (1E16) via awater discharge line (1E21). The water supply pump (1E22) is configuredto remove water (1E1), and enhancers (1E44), from the interior (1E17) ofthe water tank (1E16) for transfer downstream to be mixed with a dryenhanced feedstock (DEF) to create a wet enhanced feedstock (WEF). Thewater discharge line (1E21) is connected at one end to the water output(1E20) of the water tank (1E16) and connected at another end to thewater supply pump (1E22).

The water supply pump (1E22) pulls a suction on the water discharge line(1E21) of the water tank (1E16) and increases the pressure of the (1E1)and outputs pressurized water via a water transfer line (1E41). Thewater transfer line (1E41) has a variety of instrumentation installed onit, including: a water flow sensor (1E34); a water control valve (1E36);a third water pressure sensor (1E39); and, a water quality sensor(1E42). A second water pressure sensor (1E30) is installed on the watertransfer line (1E41) upstream of the water control valve (1E36) andcloser to the water supply pump (1E22). In embodiments, the pressuredrop across the water control valve (1E36) may range from: between about1 pound per square inch to about 5 pound per square inch; between about5 pound per square inch to about 10 pound per square inch; between about10 pound per square inch to about 15 pound per square inch; betweenabout 15 pound per square inch to about 20 pound per square inch;between about 25 pound per square inch to about 30 pound per squareinch; between about 35 pound per square inch to about 40 pound persquare inch; between about 45 pound per square inch to about 50 poundper square inch; between about 55 pound per square inch to about 60pound per square inch; between about 65 pound per square inch to about70 pound per square inch; between about 75 pound per square inch toabout 80 pound per square inch; between about 85 pound per square inchto about 90 pound per square inch; between about 95 pound per squareinch to about 100 pound per square inch; between about 100 pound persquare inch to about 125 pound per square inch; between about 125 poundper square inch to about 150 pound per square inch; or, between about150 pound per square inch to about 200 pound per square inch.

The water transfer line (1E41) is discharged from the water distributionmodule (1E) en route to the enhanced feedstock distribution module (1F)on FIGS. 24-26. The water distribution module (1E) contains a firstaccess door (1E55) at one end and a second access door (1E56) at anotherend. The water distribution module (1E) also contains an air vent (1E57)for introduction of an air supply (1E58). The water distribution module(1E) also contains a low voltage disconnect switch (1E59) and a computer(COMP)

FIG. 22

FIG. 22 shows a top view of one embodiment of a water distributionmodule (1E). Refer to the text in the preceding section for thedescription of FIG. 22.

FIG. 23

FIG. 23 shows a first side view of one embodiment of a waterdistribution module (1E). Visible from the first side view of the waterdistribution module (1E) is the first access door (1E55) along with theair vent (1E57) for introduced on an air supply (1E58). A water inputline (1E4) containing is shown entering the first water treatment unit(1E6) via a first water treatment unit input (1E7). Water (1E1) is showncontained within the interior (1E17) of the water tank (1E16). Enhancers(1E44) are shown contained within the interior (1E46) of the enhancertank (1E45).

FIG. 24

FIG. 24 shows a front view of one embodiment of an enhanced feedstockdistribution module (1F). The enhanced feedstock distribution module(1F) is shown to be contained within a 40 feet high cube containerconforming to the International Organization for Standardization (ISO)specifications. Water (1E1) enters from the left-hand-side of theenhanced feedstock distribution module (1F) via a water transfer line(1E41). The water (1E1) is mixed with a dry enhanced feedstock (DEF) toform a wet enhanced feedstock (WEF). The dry enhanced feedstock (DEF)enters from the left-hand-side of the enhanced feedstock distributionmodule (1F) via an enhanced feedstock transport screw (1A20). A wetenhanced feedstock (WEF) is transported to the enhanced feedstocksplitter (1F1) via an enhanced feedstock transfer line (1F0). Anenhanced feedstock moisture sensor (1A12B) is installed on the enhancedfeedstock transfer line (1F0). In embodiments, the wet enhancedfeedstock (WEF) may be introduced to the enhanced feedstock splitter(1F1) through an enhanced feedstock transfer line (1F0) via a pluralityof inputs (1F3A, 1F3B, 1F3C). Each of the first splitter input (1F3A),second splitter input (1F3B), and third splitter input (1F3C), transfera wet enhanced feedstock (WEF) to the interior (1F2) of the enhancedfeedstock splitter (1F1).

The enhanced feedstock splitter (1F1) has a top section (1F4), bottomsection (1F5), and an interior (1F2) defined by at least one side wall(1F6). A first splitter level sensor (1F7) is positioned on the sidewall (1F6). The enhanced feedstock splitter (1F1) is shown equipped witha splitter first screw conveyor (1F9) and a splitter second screwconveyor (1F14) both positioned at the bottom section (1F5) of theenhanced feedstock splitter (1F1). The splitter first screw conveyor(1F9) transfers enhanced feedstock from the interior (1F2) of theenhanced feedstock splitter (1F1) to a first weigh screw (1F24) via afirst output (1F10). The splitter second screw conveyor (1F14) transfersenhanced feedstock from the interior (1F2) of the enhanced feedstocksplitter (1F1) to a second weigh screw (1F33) via a second output(1F15). The enhanced feedstock distribution module (1F) is shownequipped with a low voltage disconnect switch (1F55) and a computer(COMP).

FIG. 25

FIG. 25 shows a top view of one embodiment of an enhanced feedstockdistribution module (1F). The enhanced feedstock distribution module(1F) is shown to be contained within a 40 feet high cube containerconforming to the International Organization for Standardization (ISO)specifications. Water (1E1) enters from the left-hand-side of theenhanced feedstock distribution module (1F) via a water transfer line(1E41). The water (1E1) is mixed with a dry enhanced feedstock (DEF) toform a wet enhanced feedstock (WEF). The dry enhanced feedstock (DEF)enters from the left-hand-side of the enhanced feedstock distributionmodule (1F) via an enhanced feedstock transport screw (1A20). A wetenhanced feedstock (WEF) is transported to the enhanced feedstocksplitter (1F1) via an enhanced feedstock transfer line (1F0). Anenhanced feedstock moisture sensor (1A12B) is installed on the enhancedfeedstock transfer line (1F0). In embodiments, the wet enhancedfeedstock (WEF) may be introduced to the enhanced feedstock splitter(1F1) through an enhanced feedstock transfer line (1F0) via a pluralityof inputs (1F3A, 1F3B, 1F3C). Each of the first splitter input (1F3A),second splitter input (1F3B), and third splitter input (1F3C), transfera wet enhanced feedstock (WEF) to the interior (1F2) of the enhancedfeedstock splitter (1F1).

The enhanced feedstock splitter (1F1) has an interior (1F2) defined byat least one side wall (1F6). A first splitter level sensor (1F7) ispositioned on the side wall (1F6). The enhanced feedstock splitter (1F1)is shown equipped with a splitter first screw conveyor (1F9) and asplitter second screw conveyor (1F14) both positioned within theinterior (1F2) of the enhanced feedstock splitter (1F 1).

The splitter first screw conveyor (1F9) transfers enhanced feedstockfrom the interior (1F2) of the enhanced feedstock splitter (1F1) to afirst weigh screw (1F24) via a first output (1F10). The first weighscrew (1F24) has a first weigh screw input (1F25) and a first weighscrew output (1F26). The first weigh screw input (1F25) of the firstweigh screw (1F24) accepts enhanced feedstock from the first output(1F10) of the splitter first screw conveyor (1F9). The splitter firstscrew conveyor (1F9) is equipped with a splitter first screw conveyormotor (1F11). The first weigh screw (1F24) is configured to discharge afirst weighed enhanced feedstock stream (1F32) or a first enhancedfeedstock stream (EF1) via the first weigh screw output (1F26). Thefirst weighed enhanced feedstock stream (1F32) or the first enhancedfeedstock stream (EF1) is discharged from the first weigh screw output(1F26) where it is then transferred to a first feeding chamber (FC1).The first weigh screw (1F24) is equipped with a mass sensor (1F27) and afirst weigh screw motor (1F29).

The splitter second screw conveyor (1F14) transfers enhanced feedstockfrom the interior (1F2) of the enhanced feedstock splitter (1F1) to asecond weigh screw (1F33) via a second output (1F15). The second weighscrew (1F33) has a second weigh screw input (1F34) and a second weighscrew output (1F35). The second weigh screw input (1F34) of the secondweigh screw (1F33) accepts enhanced feedstock from the second output(1F15) of the splitter second screw conveyor (1F14). The splitter secondscrew conveyor (1F14) is equipped with a splitter second screw conveyormotor (1F16). The second weigh screw (1F33) is configured to discharge asecond weighed enhanced feedstock stream (1F41) or a second enhancedfeedstock stream (EF2) via the second weigh screw output (1F35). Thesecond weighed enhanced feedstock stream (1F41) or the second enhancedfeedstock stream (EF2) is discharged from the second weigh screw output(1F35) where it is then transferred to a second feeding chamber (FC2).The second weigh screw (1F33) is equipped with a mass sensor (1F36) anda second weigh screw motor (1F38).

The enhanced feedstock distribution module (1F) is shown equipped with alow voltage disconnect switch (1F55) and a computer (COMP). Also shownis a first access door (1F51), second access door (1F52), and an airvent (1F53) configured to introduce an air supply (1F54) to the enhancedfeedstock distribution module (1F).

FIG. 26

FIG. 26 shows a first side view of one embodiment of an enhancedfeedstock distribution module (1F). Visible from the first side view ofthe enhanced feedstock transfer line (1F0) is the first access door(1F51) along with the air vent (1F53) for introduced on an air supply(1F54). The enhanced feedstock splitter (1F1) is shown to have aninterior (1F2) defined by at least one side wall (1F6). A first splitterlevel sensor (1F7) is positioned on the side wall (1F6). The enhancedfeedstock splitter (1F1) has a top section (1F4) and a bottom section(1F5). A splitter second screw conveyor (1F14) is positioned within theinterior (1F2) of the enhanced feedstock splitter (1F1) at the bottomsection (1F5).

A water transfer line (1E41) is shown entering the enhanced feedstocktransfer line (1F0) where it mixes with enhanced feedstock and is routedto the interior (1F2) of the enhanced feedstock splitter (1F1) via anenhanced feedstock transfer line (1F0) and a first splitter input(1F3A). The first splitter input (1F3A) has an insertion distance(1F3A1) positioned within the interior (1F2) of the enhanced feedstocksplitter (1F1). In embodiments, the insertion distance (1F3A1) may rangefrom: between about 2 inches to about 4 inches; between about 4 inchesto about 8 inches; between about 8 inches to about 12 inches; betweenabout 12 inches to about 16 inches; between about 16 inches to about 20inches; between about 20 inches to about 24 inches; between about 24inches to about 28 inches; between about 28 inches to about 30 inches;between about 30 inches to about 34 inches; between about 34 inches toabout 36 inches; between about 36 inches to about 40 inches; betweenabout 40 inches to about 44 inches; between about 44 inches to about 46inches; between about 46 inches to about 50 inches; or, between about 50inches to about 60 inches.

A second output (1F15) is shown at the bottom section (1F5) of theenhanced feedstock splitter (1F1). A second weigh screw (1F33) is shownto have a second weigh screw input (1F34) and a second weigh screwoutput (1F35). The second weigh screw input (1F34) is connected to thesecond output (1F15) is shown at the bottom section (1F5) of theenhanced feedstock splitter (1F1). The second weigh screw (1F33) isequipped with a mass sensor (1F36) and a second weigh screw motor(1F38). The second weighed enhanced feedstock stream (1F41) or thesecond enhanced feedstock stream (EF2) is discharged from the secondweigh screw output (1F35) where it is then transferred to a secondfeeding chamber (FC2).

FIG. 27A

FIG. 27A shows a front view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C). Referring to FIGS. 27-29, the insectfeeding module (2000, 2000A, 2000B, 2000C) is shown to be containedwithin a 40 feet high cube container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 27A shows an insect feeding module (2000, 2000A, 2000B, 2000C)containing a network (220) of cells (219) for growing insects (225). Thenetwork (220) of cells (219) has openings (222) first end (221) andopenings (224) of the second end (223). A vibration unit (214) equippedwith a vibration unit motor (215) is operatively connected to thenetwork (220) of cells (219) via a first vibration unit connection(218A) and a second vibration unit connection (218B). The vibration unit(214) is configured to vibrate at least a portion of the network (220)of cells (219) to assist in removal of insects (225) contained therein.

In embodiments, the network (220) of cells (219) has a network length(N-L) that is greater than the network width (N-W). In embodiments, thenetwork (220) of cells (219) has a network length (N-L) that is lessthan the network width (N-W). In one example, as in the non-limitingembodiments of FIGS. 27-29, the network width (N-W) is approximatelyabout between about 4 feet to about 5 feet, and the network length (N-L)is approximately about between about 30 feet to about 31 feet to fitwithin the cube container and allowing for access and maintenance. Inembodiments, the network length (N-L) ranges from: 0.5 feet to about 1foot; between about 1 feet to about 2 feet; between about 2 feet toabout 3 feet; between about 3 feet to about 4 feet; between about 4 feetto about 5 feet; between about 5 feet to about 6 feet; between about 6feet to about 7 feet; between about 7 feet to about 8 feet; betweenabout 8 feet to about 9 feet; between about 9 feet to about 10 feet;between about 10 feet to about 11 feet; between about 11 feet to about12 feet; between about 12 feet to about 13 feet; between about 13 feetto about 14 feet; between about 14 feet to about 15 feet; between about15 feet to about 16 feet; between about 16 feet to about 17 feet;between about 17 feet to about 18 feet; between about 18 feet to about19 feet; between about 19 feet to about 20 feet; between about 20 feetto about 21 feet; between about 21 feet to about 22 feet; between about22 feet to about 23 feet; between about 23 feet to about 24 feet;between about 24 feet to about 25 feet; between about 25 feet to about26 feet; between about 26 feet to about 27 feet; between about 27 feetto about 28 feet; between about 28 feet to about 29 feet; between about29 feet to about 30 feet; between about 30 feet to about 31 feet;between about 31 feet to about 32 feet; between about 32 feet to about33 feet; between about 33 feet to about 34 feet; between about 34 feetto about 35 feet; between about 35 feet to about 36 feet; between about36 feet to about 37 feet; between about 37 feet to about 38 feet;between about 38 feet to about 39 feet; and, between about 39 feet toabout 40 feet.

In embodiments, the network width (N-W) ranges from: 0.5 feet to about 1foot; between about 1 feet to about 2 feet; between about 2 feet toabout 3 feet; between about 3 feet to about 4 feet; between about 4 feetto about 5 feet; between about 5 feet to about 6 feet; between about 6feet to about 7 feet; between about 7 feet to about 8 feet; betweenabout 8 feet to about 9 feet; between about 9 feet to about 10 feet;between about 10 feet to about 11 feet; between about 11 feet to about12 feet; between about 12 feet to about 13 feet; between about 13 feetto about 14 feet; between about 14 feet to about 15 feet; between about15 feet to about 16 feet; between about 16 feet to about 17 feet;between about 17 feet to about 18 feet; between about 18 feet to about19 feet; between about 19 feet to about 20 feet; between about 20 feetto about 21 feet; between about 21 feet to about 22 feet; between about22 feet to about 23 feet; between about 23 feet to about 24 feet;between about 24 feet to about 25 feet; between about 25 feet to about26 feet; between about 26 feet to about 27 feet; between about 27 feetto about 28 feet; between about 28 feet to about 29 feet; between about29 feet to about 30 feet; between about 30 feet to about 31 feet;between about 31 feet to about 32 feet; between about 32 feet to about33 feet; between about 33 feet to about 34 feet; between about 34 feetto about 35 feet; between about 35 feet to about 36 feet; between about36 feet to about 37 feet; between about 37 feet to about 38 feet;between about 38 feet to about 39 feet; and, between about 39 feet toabout 40 feet.

In embodiments, the interior (201) of the cube container is the interior(201) of the feeding chamber (200). The first side wall (202A) of thefeeding chamber (200) is shown spaced apart from the first cubecontainer side wall (CW-A). The second side wall (202B) of the feedingchamber (200) is shown spaced apart from the second cube container sidewall (CW-B). The third side wall (202C) of the feeding chamber (200) isshown spaced apart from the third cube container side wall (CW-C). Thefourth side wall (202D) of the feeding chamber (200) is shown spacedapart from the fourth cube container side wall (CW-D).

The top (203) of the feeding chamber (200) is shown to be the cubecontainer top wall (CW-T). The first side wall (202A), second side wall(202B), third side wall (202C), fourth side wall (202D), may beflexible, perforated, wire or screen, or the like which is positionedextending into the interior (201) of the feeding chamber from the at aside wall length (SW-L). No screen floor (258) is shown in FIGS. 27-29instead the bottom (204) of the feeding chamber (200) is open to thesurface of the conveyor (255) of the egg transfer system (244).

The first side wall (202A), second side wall (202B), third side wall(202C), and fourth side wall (202D) are spaced apart from the cubecontainer side walls (CW-A, CW-B, CW-C, CW-D) so that the entireinterior (201) of the feeding chamber (200) is positioned directly abovethe conveyor (245) of the egg transfer system (244). This will allow forcomplete removal of all the contents from within the interior (201) ofthe feeding chamber (200) with the use of vibration or a vacuum or bothor none. In embodiments, when the first conveyor elevation unit (254)and second conveyor elevation unit (256) are extended at a secondelevated height (H2) there is no gap between the terminal end of theside wall length (SW-L) of each of the first side wall (202A), secondside wall (202B), third side wall (202C), and fourth side wall (202D).In embodiments, when the first conveyor elevation unit (254) and secondconveyor elevation unit (256) are extended at a second elevated height(H2) there is a gap between the terminal end of the second side walllength (202BL) only.

In embodiments, when the first conveyor elevation unit (254) and secondconveyor elevation unit (256) are extended at a second elevated height(H2) there is a gap between the terminal end of the first side walllength (202AL) and second side wall length (202BL). FIGS. 27-29 shownon-limiting embodiments of the insect feeding module (2000, 2000A,2000B, 2000C) contained within a cube container and for representativeand illustrative purposes only show the first conveyor elevation unit(254) and second conveyor elevation unit (256) at a first retractedheight (H1). Refer to above text for modes of operation and detaileddescription on the feeding chamber (200) integrated with the eggtransfer system (244).

A first weighed enhanced feedstock stream (1F32) or synonymously termedfirst enhanced feedstock stream (EF1) enters the insect feeding module(2000, 2000A) on the left-hand-side through an enhanced feedstock input(206). The enhanced feedstock input (206) transfers a wet enhancedfeedstock (WEF) onto the conveyor (245) of the egg transfer system (244)through a plurality of enhanced feedstock inputs (206A, 206B, 206C) soas to be configured to evenly distribute the enhanced feedstock on theconveyor (245). In embodiments, the third side wall length (202CL) andfourth side wall length (202DL) are longer than the first side walllength (202AL) and second side wall length (202BL) so as to leave a gapin between the conveyor (245) and the terminal end of the first sidewall length (202AL) and second side wall length (202BL). In embodiments,the first side wall length (202AL), second side wall length (202BL),third side wall length (202CL), fourth side wall length (202DL), rangein between about 5 feet to about 6 feet so they may fit within the cubecontainer for interaction with the conveyor (245) of the egg transfersystem (244).

In embodiments, the first side wall length (202AL), second side walllength (202BL), third side wall length (202CL), fourth side wall length(202DL), range from: 0.5 feet to about 1 foot; between about 1 feet toabout 2 feet; between about 2 feet to about 3 feet; between about 3 feetto about 4 feet; between about 4 feet to about 5 feet; between about 5feet to about 6 feet; between about 6 feet to about 7 feet; betweenabout 7 feet to about 8 feet; between about 8 feet to about 9 feet;between about 9 feet to about 10 feet; between about 10 feet to about 11feet; between about 11 feet to about 12 feet; between about 12 feet toabout 13 feet; between about 13 feet to about 14 feet; between about 14feet to about 15 feet; between about 15 feet to about 16 feet; betweenabout 16 feet to about 17 feet; between about 17 feet to about 18 feet;between about 18 feet to about 19 feet; between about 19 feet to about20 feet; between about 20 feet to about 21 feet; between about 21 feetto about 22 feet; between about 22 feet to about 23 feet; between about23 feet to about 24 feet; between about 24 feet to about 25 feet;between about 25 feet to about 26 feet; between about 26 feet to about27 feet; between about 27 feet to about 28 feet; between about 28 feetto about 29 feet; between about 29 feet to about 30 feet; between about30 feet to about 31 feet; between about 31 feet to about 32 feet;between about 32 feet to about 33 feet; between about 33 feet to about34 feet; between about 34 feet to about 35 feet; between about 35 feetto about 36 feet; between about 36 feet to about 37 feet; between about37 feet to about 38 feet; between about 38 feet to about 39 feet; and,between about 39 feet to about 40 feet.

In embodiments, the first side wall (202A), second side wall (202B),third side wall (202C), and fourth side wall (202D) are made up of wire,screen, or mesh that is perforated with openings smaller than theaverage insect length (Ni-L) average insect width (Ni-W). Inembodiments, the first side wall (202A), second side wall (202B), thirdside wall (202C), and fourth side wall (202D) are made up of a plastic,rubber, or an impermeable substance, such as a tarp, curtain, cloth, orsheet and does not have openings in it.

An egg-depleted breeding material (246) enters the insect feeding module(2000, 2000A) on the left-hand-side through a conveyor input (247).Egg-depleted breeding material (246) is transferred onto the conveyor(245) of the egg transfer system (244) through a plurality of conveyorinputs (247A, 247B) so as to be configured to evenly distribute theenhanced feedstock on the conveyor (245). The wet enhanced feedstock(WEF) and the egg-depleted breeding material (246) are mixed together onthe surface of the conveyor (245) of the egg transfer system (244).

As the conveyor motor (251) drives the conveyor (245) of the eggtransfer system (244). Insects (225) within the insect feeding chamber(200) eat the wet enhanced feedstock (WEF) and lay eggs in theegg-depleted breeding material (246) which are both present on theconveyor (245) of the egg transfer system (244). The conveyor output(249) discharges a mixture of wet enhanced feedstock (WEF) and egg-ladenbreeding material (250) towards an egg-laden breeding material conveyor(282B) for transfer to a breeding chamber (BC) within an insect breedingmodule (4000, 4000A, 4000B, 4000C). A conveyor transfer bin (282A) isinstalled in between the conveyor output (249) to funnel and direct themixture of wet enhanced feedstock (WEF) and egg-laden breeding material(250) towards the egg-laden breeding material conveyor (282B).

An air supply fan (271) accepts an air supply (262) through an air vent(283) and passes it through an air heater (264) for delivery into theinterior (201) of the feeding chamber (200). A first access door (284)and a second access door (285) are installed on the fourth cubecontainer side wall (CW-D). An insect evacuation output (205), that isconfigured to evacuate an insect and gas mixture (304) from the feedingchamber (200), is shown installed on the cube container top wall (CW-T).The insect evacuation output (205) is connected to the feeding chamberexit conduit (302). The feeding chamber exit conduit (302) is connectedto the insect and gas mixture input (303) of the separator (300) withinthe insect evacuation module (3000). Each insect feeding module (2000,2000A, 2000B, 2000C) may be equipped with a low voltage disconnectswitch (286) and a computer (COMP). The insect evacuation output (205)is equipped with a humidity sensor (208) and a first temperature sensor(210).

FIG. 28A

FIG. 28A shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C).

FIG. 27B

FIG. 27B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one cube container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIGS. 27B and 28B show a front view and a side view of one non-limitingembodiment where a plurality of feeding chambers are provided in onecube container conforming to the International Organization forStandardization (ISO) specifications. In embodiments, the cube containerof FIG. 27B and FIG. 28B are a 20 foot high. In embodiments, the cubecontainer of FIG. 27B and FIG. 28B are a 40 foot high.

FIG. 27B and FIG. 28B further elaborate upon FIG. 27A and FIG. 28Aexcept including a first feeding chamber (FC1, 200-1) and a secondfeeding chamber (FC2, 200-2) within the same cube container. FIG. 27Band FIG. 28B only show two feeding chambers (FC1, FC2) within one cubecontainer, however it is to be noted that more than two may also be usedas well.

The first feeding chamber (FC1) has a first insect evacuation output(205-1) and a feeding chamber first exit conduit (302-1) that areconfigured to discharge a first insect and gas mixture (304-1). Thesecond feeding chamber (FC2) has a second insect evacuation output(205-2) and a feeding chamber second exit conduit (302-2) that areconfigured to discharge a second insect and gas mixture (304-2). Thefirst feeding chamber (FC1) has a first side wall (202A), second sidewall (202B), third side wall (202C), and a fourth side wall (202D). Thesecond feeding chamber (FC2) has a first side wall (202AA), second sidewall (202BB), third side wall (202CC), and a fourth side wall (202DD).

As seen in FIG. 27B and FIG. 28B, the second side wall (202B) of thefirst feeding chamber (FC1) is the first side wall (202AA) of the secondfeeding chamber (FC2). The first feeding chamber (200-1) has a firstnetwork length (N-L1) and a first network width (N-W1). The secondfeeding chamber (200-2) has a second network length (N-L2) and a secondnetwork width (N-W2). The first feeding chamber (200-1) has a firstvibration unit connection (218A). The second feeding chamber (200-2) hasa second vibration unit connection (218B).

FIG. 27C

FIG. 27C shows a top view of one embodiment of an insect feeding module(2000, 24000A, 2000B, 2000C) equipped with a humidity control unit(HCU).

FIG. 27C shows a non-limiting embodiment of a humidity control unit(HCU) positioned within the interior (201) of the feeding chamber (200).FIG. 27C also shows a humidity control unit (HCU) positioned within theinterior (201) of the feeding chamber (200, FC1, FC2, FC3) that iscontained within a cube container.

In embodiments, the humidity control unit (HCU) includes a compressor(Q30), a condenser (Q32), a metering device (Q33), an evaporator (Q34),and a fan (Q35). The fan (Q35) may be equipped with a motor (Q36) and acontroller (Q37) that is configured to input or output a signal (Q38) toa computer (COMP).

The compressor (Q31) is connected to the condenser (Q32), the condenser(Q32) is connected to the metering device (Q33), the metering device(Q33) is connected to an evaporator (Q34), and the evaporator (Q34) isconnected to the compressor (Q31) to form a closed-loop refrigerationcircuit configured to contain a refrigerant (Q31). The metering device(Q33) includes one or more from the group consisting of a restriction,orifice, valve, tube, capillary, and capillary tube. The refrigerant(Q31) is conveyed from the compressor to the condenser, from thecondenser to the evaporator through the metering device, and from theevaporator to the compressor. The evaporator (Q34) is positioned toremove humidity from within the interior (201) of the feeding chamber(200, FC1, FC2, FC3) and is configured to evaporate refrigerant (Q31)within the evaporator (Q34) by removing heat from the interior (201) ofthe feeding chamber (200, FC1, FC2, FC3). In embodiments, a portion ofthe evaporator (Q34) is contained within the interior (201) of thefeeding chamber 200, FC1, FC2, FC3).

In embodiments, a portion of the evaporator (Q34) is contained withinthe interior (201) of an enclosure, such as a cube container, that thefeeding chamber (200, FC1, FC2, FC3) is positioned within. Inembodiments, the condenser (Q32) is not contained within the interior(201) of the feeding chamber (200, FC1, FC2, FC3). The fan (Q35) isconfigured to blow air from within the interior (201) of the feedingchamber (200, FC1, FC2, FC3) over at least a portion of the humiditycontrol unit (HCU).

The humidity control unit (HCU) is configured to selectively operate thesystem in a plurality of modes of operation, the modes of operationincluding at least:

(1) a first mode of operation in which compression of a refrigerant(Q31) takes place within the compressor (Q30), and the refrigerant (Q31)leaves the compressor (Q30) as a superheated vapor at a temperatureabove the condensing point of the refrigerant (Q31);

(2) a second mode of operation in which condensation of refrigerant(Q31) takes place within the condenser (Q32), heat is rejected and therefrigerant (Q31) condenses from a superheated vapor into a liquid, andthe liquid is cooled to a temperature below the boiling temperature ofthe refrigerant (Q31); and

(3) a third mode of operation in which evaporation of the refrigerant(Q31) takes place, and the liquid phase refrigerant (Q31) boils inevaporator (Q34) to form a vapor or a superheated vapor while absorbingheat from the interior (201) of the feeding chamber (200).

The evaporator (Q34) is configured to evaporate the refrigerant (Q31) toabsorb heat from the interior (201) of the feeding chamber (200). As aresult, the evaporator (Q34) may condense water from the interior (201)of the feeding chamber (200). In embodiments, the evaporator (Q34)condenses water vapor from the interior (201) of the feeding chamber(200) and forms condensate (Q39).

FIG. 28B

FIG. 28B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one cube container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 29

FIG. 29 shows a first side view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C).

FIG. 30

FIG. 30 shows a front view of one embodiment of an insect evacuationmodule (3000). FIG. 30 shows a front view of one embodiment of an insectevacuation module (3000). Referring to FIGS. 30-32, the insectevacuation module (3000) is shown to be contained within a 40 feet highcube container conforming to the International Organization forStandardization (ISO) specifications.

The insect evacuation module (3000) includes a plurality of separators(S1, S2, S3) integrated with one common feeding chamber (FC1) as shownin FIGS. 27-29. FIGS. 30-32 shows the first separator (S1) as a firstinsect coarse separator (S1A), the second separator (S2) as a secondinsect fine separator (S2A), and the third separator (S3) as aparticulate separator (S3A). The first insect coarse separator (S1A) isconfigured to remove a portion of the insect portion (304A) separatedfrom the gas portion (304B) of an insect and gas mixture (304). Thesecond insect fine separator (S2A) is configured to remove insectssmaller than the insects separated in the first insect coarse separator(S1A). The particulate separator (S3A) is configured to removeparticulates such as remnants of enhanced feedstock, or fine polymerparticulate, for example, not only including pieces of portions ofinsect exoskeleton. The particulate separator (S3A) is in fluidcommunication with the polymer distribution module (1D) and isconfigured to transfer a portion of the separated particulate to thepolymer tank (1D2) as polymer (1D1).

First Separator (S1), First Insect Coarse Separator (S1A)

The first insect coarse separator (S1A) has a first insect coarseseparator input (S1A1) that is in fluid communication with the firstfeeding chamber insect evacuation output (205A) of the first feedingchamber (FC1) via a first feeding chamber exit conduit (302A). The firstinsect coarse separator (S1A) is configured to accept an insect and gasmixture (304) from the first feeding chamber (FC1), separate a portionof the insects from the gas and output a first insect-depleted gasstream (355) via a coarse separator gas and insect mixture output (356).

The first separator (S1) is equipped with a first dipleg (357), a firstseparator conveyor (358), and a first separator valve (361) interposedon the first dipleg (357). A first separated insect stream (360) isrouted down the first dipleg (357), through the first separator valve(361) and into the first separator conveyor (358). In embodiments, thefirst separator conveyor (358) is a compression screw (359) which servesto instantly kill insects by compressing them. The first separatedinsect stream (360) may in turn be transferred to an evacuated separatedinsect conveyor (378) via a first separator conveyor connection (379).

The evacuated separated insect conveyor (378) has a motor (378A) that isconfigured to transfer the first separated insect stream (360) to agrinder (1250) within an insect grinding module via a first separatedinsect stream input (371). In other embodiments, the first separatedinsect stream (360) may be sent to a pathogen removal unit (1550) withina pathogen removal module, or to a within a lipid extraction unit (1501)lipid extraction module.

Second Separator (S2), Second Insect Fine Separator (S2A)

The second insect fine separator (S2A) has a second insect fineseparator input (S2A1) that is in fluid communication with the coarseseparator gas and insect mixture output (356) of the first insect coarseseparator (S1A). The second insect fine separator (S2A) is configured toaccept a first insect-depleted gas stream (355) from the first insectcoarse separator (S1A), separate a portion of the insects from the gasand output a second insect-depleted gas stream (362) via a fineseparator gas and particulate mixture output (363).

The second separator (S2) is equipped with a second dipleg (364), asecond separator conveyor (365), and a second separator valve (368)interposed on the second dipleg (364). A second separated insect stream(360) is routed down the second dipleg (364), through the secondseparator valve (368) and into the second separator conveyor (365). Inembodiments, the second separator conveyor (365) is a compression screw(366) which serves to instantly kill insects by compressing them.

In embodiments, the second separator conveyor (365) is a not acompression screw (366) but instead routes the second separated insectstream (367) to the to a breeding chamber (BC) via a breeding chamberfine separated insect portion input (375). In embodiments, the secondseparator conveyor (365) is a not a compression screw (366) but insteadroutes the second separated insect stream (367) to a plurality of otherdestinations such as to the grinder (1250), pathogen removal unit(1550), or lipid extraction unit (1501). The second separated insectstream (367) may in turn be transferred to an evacuated separated insectconveyor (378) via a second separator conveyor connection (380) to forma combined first and second separator insect stream (381).

The combined first and second separator insect stream (381) is a mixtureof the first separated insect stream (360) and the second separatedinsect stream (367). The evacuated separated insect conveyor (378) has amotor (378A) that is configured to transfer the combined first andsecond separator insect stream (381) to a grinder (1250) within aninsect grinding module via a first separated insect stream input (371).In other embodiments, the first separated insect stream (360) may besent to a pathogen removal unit (1550) within a pathogen removal module,or to a within a lipid extraction unit (1501) lipid extraction module.

Third Separator (S3), Particulate Separator (S3A)

The particulate separator (S3A) has a particulate separator input (S3A1)that is in fluid communication with the fine separator gas andparticulate mixture output (363) of the second insect fine separator(S2A). The particulate separator (S3A) is configured to accept a secondinsect-depleted gas stream (362) from the second insect fine separator(S2A), separate a portion of the particulates from the gas and output aparticulate-depleted gas stream (369) to the insect evacuation fan(312).

The insect evacuation fan (312) is in fluid with the breeding chamber(BC) via a breeding chamber exhaust input (376) and is configured todischarge the exhaust (377) into the breeding chamber (BC). Inembodiments, the separated insect conveyor (328) of the third separator(S3) particulate separator (S3A) is in fluid communication with thepolymer distribution module (1D) and is configured to transfer a portionof the separated particulate stream (370) to the polymer tank (1D2) aspolymer (1D1).

In embodiments, the separated insect conveyor (328) of the thirdseparator (S3) particulate separator (S3A) is in fluid communicationwith the polymer distribution module (1D) and is configured to transfera portion of the separated particulate stream (370) to the polymer tank(1D2) as a polymer (1D1). The insect evacuation module (3000) isequipped with a first access door (386), second access door (387),computer (COMP), low voltage disconnect switch (388), and an air vent(389) that is configured to accept an air supply (390).

FIG. 31

FIG. 31 shows a top view of one embodiment of an insect evacuationmodule (3000).

FIG. 32

FIG. 32 shows a first side view of one embodiment of an insectevacuation module (3000).

FIG. 33

FIG. 33 shows a front view of one embodiment of an insect breedingmodule (4000, 4000A, 4000B, 4000C). Referring to FIGS. 33-36, the insectbreeding module (4000, 4000A, 4000B, 4000C) is shown to be containedwithin a 40 feet high cube container conforming to the InternationalOrganization for Standardization (ISO) specifications.

A feeding chamber 1 egg-laden breeding material transfer line (R1, 340)transfers egg-laden breeding material (250) via an egg-laden breedingmaterial conveyor (282B) into the insect breeding module (4000, 4000A)from the left-hand-side. Egg-laden breeding material (250), andoptionally a mixture of egg-laden breeding material (250) and a wetenhanced feedstock (WEF), are distributed onto a lower conveyor belt(415) of a first conveyor transfer unit (XY1A). The egg-laden breedingmaterial (250) being transferred to the interior (BCIN) of the breedingchamber 1 (BC1) where it is first elevated via a first conveyor transferunit (XY1A) to the first conveyor height (CH1A) of a first conveyor(CY1A) operating in a clockwise motion of operation.

In embodiments, the breeding chamber (BC) shown in FIGS. 33-36 representa typical breeding chamber 1 (BC1), breeding chamber 2 (BC2), breedingchamber 3 (BC3) as shown in FIG. 17. In embodiments, the first conveyortransfer unit (XY1A) takes the form of a vertical lift conveyor (409)including a lower conveyor unit (410) and an upper conveyor unit (411).The vertical lift conveyor (409) is equipped with a lift conveyor driveunit (419) that is configured to rotate the rollers within the lowerconveyor unit (410) and upper conveyor unit (411).

The lower conveyor unit (410) includes a first lower conveyor roller(412), second lower conveyor roller (413), third lower conveyor roller(414), and an endless lower conveyor belt (415) in communication witheach roller (412, 423, 414) and the lift conveyor drive unit (419). Theupper conveyor unit (411) includes a first upper conveyor belt roller(416), second upper conveyor roller (417), and an endless upper conveyorbelt (418) in communication with each roller (416, 417) and the liftconveyor drive unit (419).

Egg-laden breeding material (250), and optionally a mixture of egg-ladenbreeding material (250) and a wet enhanced feedstock (WEF) aredistributed onto the lower conveyor belt (415) of the lower conveyorunit (410). The breeding material and enhanced feedstock remnants aresandwiched in between the lower conveyor belt (415) of the lowerconveyor unit (410) and the upper conveyor belt (418) of the upperconveyor unit (411) and is elevated to the first conveyor height (CH1A)of a first conveyor (CY1A) operating in a clockwise motion of operation.

The first conveyor (CY1A) is positioned at a vertical height above atleast one other conveyor. FIGS. 33-36 shows five conveyors (CY1A, CY2A,CY3A, CY4A, CY5A) and the first conveyor (CY1A) is positioned at avertical height above each one of a second conveyor (CY2A), thirdconveyor (CY3A), fourth conveyor (CY4A), and fifth conveyor (CY5A). Thesecond conveyor (CY2A) is positioned at a vertical height above each oneof a third conveyor (CY3A), fourth conveyor (CY4A), and fifth conveyor(CY5A). The third conveyor (CY3A) is positioned at a vertical heightabove each one of a fourth conveyor (CY4A), and fifth conveyor (CY5A).The fourth conveyor (CY4A) is positioned at a vertical height above eachone of the fifth conveyor (CY5A).

The first conveyor (CY1A) is installed at a first conveyor height (CH1A)above the second conveyor (CY2A). The second conveyor (CY2A) isinstalled at a second conveyor height (CH2A) above the third conveyor(CY3A). The third conveyor (CY3A) is installed at a third conveyorheight (CH3A) above the fourth conveyor (CY4A). The fourth conveyor(CY4A) is installed at a fourth conveyor height (CH4A) above the fifthconveyor (CY5A).

FIG. 33-36 shows the first conveyor (CY1A), third conveyor (CY3A), fifthconveyor (CY5A) all configured to operate in a clockwise motion ofoperation. FIG. 33-36 shows the second conveyor (CY2A) and fourthconveyor (CY4A) configured to operate in a counter-clockwise motion ofoperation.

The first conveyor (CY1A) rotates in a clockwise motion about a firstconveyor first roller (P1) and a first conveyor second roller (P2). Thesecond conveyor (CY2A) rotates in a counter-clockwise motion about asecond conveyor first roller (P3) and a second conveyor second roller(P4). The third conveyor (CY3A) rotates in a clockwise motion about athird conveyor first roller (P5) and a third conveyor second roller(P6). The fourth conveyor (CY4A) rotates in a counter-clockwise motionabout a fourth conveyor first roller (P7) and a fourth conveyor secondroller (P8). The fifth conveyor (CY5A) rotates in a clockwise motionabout a fifth conveyor first roller (P9) and a fifth conveyor secondroller (P10).

A drive unit (404) is equipped with a motor (405) to drive a sprocket(406) and a roller (407). The drive unit (404) is operatively connectedto the first conveyor first roller (P1) of the first conveyor (CY1A),second conveyor second roller (P4) of the second conveyor (CY2A), thethird conveyor first roller (P5) of the third conveyor (CY3A), thefourth conveyor second roller (P8) of the fourth conveyor (CY4A), andthe fifth conveyor first roller (P9) of the fifth conveyor (CY5A).

Specifically, the sprocket (406) driven by the motor (405) of the driveunit (404) drives a roller chain (408) that is configured to operateeach conveyor (CY1A, CY2A, CY3A, CY4A, CY5A). The roller chain (408) isconfigured to interact with a roller chain support roller (P11) inbetween the first conveyor first roller (P1) and sprocket (406) of thedrive unit (404).

The circuit including the roller chain (408), sprocket (406), and driveunit (404) turns the fifth conveyor first roller (P9), third conveyorfirst roller (P5), and first conveyor first roller (P1) in the clockwisemotion. The circuit including the roller chain (408), sprocket (406),and drive unit (404) also turns the fourth conveyor second roller (P8)and second conveyor second roller (P4) in the counter-clockwise motion.

The first conveyor (CY1A) transfers a mixture of egg-laden breedingmaterial (250) and remnants of an enhanced feedstock to the secondconveyor (CY2A). The second conveyor (CY2A) transfers a mixture ofegg-laden breeding material (250) and remnants of an enhanced feedstock,and possibly hatched insects to the third conveyor (CY3A). The thirdconveyor (CY3A) transfers a mixture of egg-laden breeding material(250), remnants of an enhanced feedstock, and possibly hatched insectsto the fourth conveyor (CY4A). The fourth conveyor (CY4A) transfers amixture of egg-laden breeding material (250), remnants of an enhancedfeedstock, and possibly hatched insects to the fifth conveyor (CY5A).The fifth conveyor (CY5A) transfers a mixture of hatched insects,breeding material, and remnants of an enhanced feedstock to a hatchedinsect conveyor (402) and out of the insect breeding module (4000,4000A, 4000B, 4000C) via a feeding chamber 1 breeding chamber output(BC1B).

A conveyor transfer bin (401) is interposed in between the fifthconveyor (CY5A) and the hatched insect conveyor (402) to funnel anddirect a mixture of hatched insects, breeding material, and remnants ofan enhanced feedstock from the insect breeding module (4000, 4000A,4000B, 4000C) and into the hatched insect separation module (5000).

A conveyor side view (CSV) may be viewed in FIGS. 35-36 from the lengthalong the insect breeding module (4000) conveyor (CY1A, CY2A, CY3A,CY4A, CY5A). The insect breeding module (4000, 4000A, 4000B, 4000C) isequipped with a first access door (420), second access door (421), lowvoltage disconnect switch (422), temperature sensor (423), humiditysensor (425), and an air vent (427) configured to introduce an airsupply (428) to the interior (BCIN) of the breeding chamber (BC). Theinsect breeding module (4000, 4000A, 4000B, 4000C) may also be equippedwith a temperature control unit (429) to maintain a constant temperaturewith the interior (BCIN) of the breeding chamber (BC).

The first conveyor (CY1A) is equipped with a first hatched insectdetection sensor (OS1) to determine if insects have hatched and areactive on the surface of the first conveyor (CY1A). The second conveyor(CY2A) is equipped with a second hatched insect detection sensor (OS2)to determine if insects have hatched and are active on the surface ofthe second conveyor (CY2A). The third conveyor (CY3A) is equipped with athird hatched insect detection sensor (OS3) to determine if insects havehatched and are active on the surface of the third conveyor (CY3A). Thefourth conveyor (CY4A) is equipped with a fourth hatched insectdetection sensor (OS4) to determine if insects have hatched and areactive on the surface of the fourth conveyor (CY4A). The fifth conveyor(CY5A) is equipped with a fifth hatched insect detection sensor (OS5) todetermine if insects have hatched and are active on the surface of thefifth conveyor (CY5A). Either of the hatched insect detection sensors(OS1, OS2, OS3, OS4, OS5) may be an optical sensor, digital camera,motion sensor, active infrared (AIRs) sensor, passive infrared (PIRs)sensor, microwave motion sensor, continuous wave radar motion sensor(CW), vibration motion sensor, IR sensor, ultrasonic sensor, proximitysensor, and touch sensor, mass sensor, laser sensor, or the like.

FIG. 34

FIG. 34 shows a top view of one embodiment of an insect breeding module(4000, 4000A, 4000B, 4000C). A side wall (403) may be positioned in theinsect breeding module (4000, 4000A, 4000B, 4000C) to permit access andmaintenance as shown in FIGS. 34-35. In embodiments, the side wall (403)is made up of a plastic, rubber, or an impermeable substance, such as atarp, curtain, cloth, or sheet and does not have openings in it. Inembodiments, the side wall (403) is made up of wire, screen, or meshthat is perforated with openings smaller than the average insect length(Ni-L) average insect width (Ni-W).

FIG. 34A

FIG. 34A shows a top view of one embodiment of an insect breeding module(4000, 4000A, 4000B, 4000C) equipped with a humidity control unit (HCU).

FIG. 34A shows a non-limiting embodiment of a humidity control unit(HCU) positioned within the interior (BCIN) of the breeding chamber(BC). FIG. 36A also shows a humidity control unit (HCU) positionedwithin the interior (BCIN) of the breeding chamber (BC) that iscontained within a cube container.

In embodiments, the humidity control unit (HCU) includes a compressor(QQ30), a condenser (QQ32), a metering device (QQ33), an evaporator(Q34), and a fan (Q35). The fan (Q35) may be equipped with a motor(QQ36) and a controller (QQ37) that is configured to input or output asignal (QQ38) to a computer (COMP).

The compressor (QQ31) is connected to the condenser (QQ32), thecondenser (QQ32) is connected to the metering device (QQ33), themetering device (QQ33) is connected to an evaporator (QQ34), and theevaporator (QQ34) is connected to the compressor (QQ31) to form aclosed-loop refrigeration circuit configured to contain a refrigerant(QQ31). The metering device (QQ33) includes one or more from the groupconsisting of a restriction, orifice, valve, tube, capillary, andcapillary tube. The refrigerant (QQ31) is conveyed from the compressorto the condenser, from the condenser to the evaporator through themetering device, and from the evaporator to the compressor. Theevaporator (QQ34) is positioned to remove humidity from within theinterior (BCIN) of the breeding chamber (BC) and is configured toevaporate refrigerant (QQ31) within the evaporator (QQ34) by removingheat from the interior (BCIN) of the breeding chamber (BC). Inembodiments, a portion of the evaporator (QQ34) is contained within theinterior (BCIN) of the breeding chamber (BC).

In embodiments, a portion of the evaporator (QQ34) is contained withinthe interior (BCIN) of an enclosure, such as a cube container, that thebreeding chamber (BC) is positioned within. In embodiments, thecondenser (QQ32) is not contained within the interior (BCIN) of thebreeding chamber (BC). The fan (QQ35) is configured to blow air fromwithin the interior (BCIN) of the breeding chamber (BC) over at least aportion of the humidity control unit (HCU).

The humidity control unit (HCU) is configured to selectively operate thesystem in a plurality of modes of operation, the modes of operationincluding at least:

(1) a first mode of operation in which compression of a refrigerant(QQ31) takes place within the compressor (QQ30), and the refrigerant(QQ31) leaves the compressor (QQ30) as a superheated vapor at atemperature above the condensing point of the refrigerant (QQ31);

(2) a second mode of operation in which condensation of refrigerant(QQ31) takes place within the condenser (QQ32), heat is rejected and therefrigerant (QQ31) condenses from a superheated vapor into a liquid, andthe liquid is cooled to a temperature below the boiling temperature ofthe refrigerant (QQ31); and

(3) a third mode of operation in which evaporation of the refrigerant(QQ31) takes place, and the liquid phase refrigerant (QQ31) boils inevaporator (QQ34) to form a vapor or a superheated vapor while absorbingheat from the interior (BCIN) of the breeding chamber (BC).

The evaporator (QQ34) is configured to evaporate the refrigerant (QQ31)to absorb heat from the interior (BCIN) of the breeding chamber (BC). Asa result, the evaporator (QQ34) may condense water from the interior(BCIN) of the breeding chamber (BC). In embodiments, the evaporator(QQ34) condenses water vapor from the interior (BCIN) of the breedingchamber (BC) and forms condensate (QQ39).

FIG. 35

FIG. 35 shows a first side view of one embodiment of an insect breedingmodule (4000, 4000A) at a cutaway section of the conveyor side view(CSV). In embodiments, the breeding chamber (BC) includes a plurality ofconveyors including a first conveyor (CY1A), second conveyor (CY2A),third conveyor (CY3A), fourth conveyor (CY4A), and fifth conveyor (CY5A)that are operatively rotated by a plurality of rollers including a firstconveyor first roller (P1), second conveyor second roller (P4), thirdconveyor first roller (P5), fourth conveyor second roller (P8), andfifth conveyor first roller (P9).

FIG. 36

FIG. 36 shows an embodiment of the insect breeding module (4000, 4000A,4000B, 4000C) from the conveyor side view (CSV). A side wall (403) maybe positioned within the insect breeding module (4000, 4000A, 4000B,4000C) to permit a plurality of breeding trains within one since cubecontainer to be separated apart from the temperature control unit (429).Three separate breeding chamber conveyor trains are illustrated with aside wall (403) positioned to space-apart the breeding chamber conveyortrains (BCT1, BCT2, BCT3) from the temperature control unit (429).

A first breeding chamber conveyor train (BCT1) includes a plurality ofconveyors driven by a plurality of rollers including a first conveyorfirst roller (P1), second conveyor second roller (P4), third conveyorfirst roller (P5), fourth conveyor second roller (P8), and fifthconveyor first roller (P9). A second breeding chamber conveyor train(BCT2) includes a plurality of conveyors driven by a plurality ofrollers including a first conveyor first roller (P1B), second conveyorsecond roller (P4B), third conveyor first roller (P5B), fourth conveyorsecond roller (P8B), and a fifth conveyor first roller (P9B). A thirdbreeding chamber conveyor train (BCT3) includes a plurality of conveyorsdriven by a plurality of rollers including a first conveyor first roller(PIC), second conveyor second roller (P4C), third conveyor first roller(P5C), fourth conveyor second roller (P8C), and fifth conveyor firstroller (P9C).

FIG. 37

FIG. 37 shows a front view of one embodiment of a hatched insectseparation module (5000, 5000A, 5000B, 5000C). Referring to FIGS. 37-39,the hatched insect separation module (5000, 5000A, 5000B, 5000C) isshown to be contained within a 40 feet high cube container conforming tothe International Organization for Standardization (ISO) specifications.

FIGS. 37-39 shows the hatched insect separation module (5000) equippedwith a breeding material and insect separator (SEPIA) and a breedingmaterial tank (500). A hatched insect conveyor (402) transfers a mixtureof hatched insects, breeding material, and remnants of an enhancedfeedstock into a breeding material and insect separator (SEPIA) via ahatched insect and breeding material input (515).

The breeding material and insect separator (SEPIA) includes an interior(SIN1), a separator input (1SEPA), a separator material output (1SEPB),and a separator insect output (1SEPC). The breeding material and insectseparator (SEPIA) is connected to breeding chamber 1 (BC1) via abreeding chamber 1 hatched egg and breeding material transfer line (U1).The breeding chamber 1 hatched egg and breeding material transfer line(U1) is connected at one end to the breeding chamber 1 (BC1) via afeeding chamber 1 breeding chamber output (BC1B) and connected atanother end to the breeding material and insect separator (SEPIA) via aseparator input (1SEPA).

The breeding material and insect separator (SEPIA) is equipped with adipleg (517) to transfer an egg-depleted material (518) to anegg-depleted material transfer conveyor (519). The egg-depleted materialtransfer conveyor (519) is equipped with a motor (520) and is configuredto transfer separated breeding material (523) to the interior (501) ofthe breeding material tank (500) via a material transfer line (522). Thematerial transfer line (522) is connected at one end to the egg-depletedmaterial transfer conveyor (519) and at another rend to the breedingmaterial input (502) of the breeding material tank (500).

The separator input (1SEPA) is configured to accept hatched insects andbreeding material from the fifth conveyor (CY5A) of breeding chamber 1(BC1), and separate hatched insects (400) from the breeding material(523). The separator insect output (1SEPC) is configured to dischargehatched insects (400) from the interior (SIN1) of the breeding materialand insect separator (SEPIA) and route the hatched insects (400) toeither one of a plurality of feeding chambers (FC1, FC2, FC3) via aseparator hatched insect transfer line (O1). Specifically, separatorinsect output (1SEPC) is configured to discharge hatched insects (400)first feeding chamber (FC1), or to the second feeding chamber (FC2), orto the third feeding chamber (FC3). Hatched insects (400) transferredfrom the hatched insect separation module (5000) to the insect feedingmodule (2000) are made available to the first feeding chamber (FC1) viaa first hatched insect output (DFC).

The breeding material tank (500) has an interior (501), a breedingmaterial input (502), and a breeding material output (510). Breedingmaterial, and remnants of an enhanced feedstock may be transferred fromthe breeding material and insect separator (SEPIA) interior (501) of thebreeding material tank (500) through a breeding material input (502).Breeding material, and remnants of an enhanced feedstock may besubstantially evenly distributed to the interior (501) of the breedingmaterial tank (500) via a breeding material input distributor (502A).

The breeding material tank (500) also has a top section (503), a bottomsection (506), and an interior (501) defined by at least one side wall(507). A breeding material screw conveyor (508) is located at the bottomsection (506) and configured to transfer breeding material to either oneof a plurality of feeding chambers (FC1, FC2, FC3) via a breedingmaterial transfer line (511). The breeding material transfer line (511)is connected at one end to any one of a plurality of feeding chambers(FC1, FC2, FC3) and connected at another end to the breeding materialscrew conveyor (508) via a breeding material output (510). The breedingmaterial screw conveyor (508) is equipped with a breeding material screwconveyor motor (512). The hatched insect separation module (5000) isequipped with a first access door (528), second access door (529), lowvoltage disconnect switch (530), and a computer (COMP).

FIG. 38

FIG. 38 shows a top view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 39

FIG. 39 shows a first side view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 40A

FIG. 40 shows Table 1 with upper and lower ranges of feedstock mineralenhancers, feedstock vitamin enhancers, feedstock polymer enhancers, andother ‘Energy-Insect™’ enhancers.

FIG. 40B

FIG. 40B shows one non-limiting example of process conditions within anInsect Production Superstructure System (IPSS). Table 2 of FIG. 40Blists process conditions including the following: Feeding ChamberTemperature ranges from between about 60 degrees Fahrenheit to about 94degrees Fahrenheit; Breeding Chamber Temperature ranges from betweenabout 64 degrees Fahrenheit to about 90 degrees Fahrenheit; BreedingChamber Residence Time ranges from between about 1 week to about 5weeks; Feeding Chamber Humidity ranges from between about 25 percenthumidity to about 100 percent humidity; Breeding Chamber Humidity rangesfrom between about 50 percent humidity to about 100 percent humidity;average insect mass ranges from between about 0.2 grams to about 0.907grams; quantity of insects per pound ranges from between about 2268insects to about 500 insects; tons of insects per cycle ranges frombetween about 0.5 ton to about 1 ton; quantity of insects per cycleranges from between about 2,267,950 to about 1,000,000; and, durationper cycle ranges from between about 1 week to about 5 weeks. Inembodiments, a cycle may be defined as the duration of time when insectsare grown within the feeding chamber or plurality of feeding chambers.

FIG. 40C

FIG. 40C shows nutritional requirements of insects produced in an InsectProduction Superstructure System (IPSS) that are fed an enhancedfeedstock. Table 3 of FIG. 40C lists nutritional information for insectsfed an enhanced feedstock within an Insect Production SuperstructureSystem (IPSS) including the following: energy content ranges frombetween about 4,500 British Thermal Units (BTU) per pound to about10,500 BTU per pound; protein content ranges from between about 45weight percent to about 85 weight percent; carbon content ranges frombetween about 15 weight percent to about 55 weight percent; oxygencontent ranges from between about 15 weight percent to about 55 weightpercent; hydrogen content ranges from between about 2.5 weight percentto about 20 weight percent; carbohydrate content ranges from betweenabout 3.5 weight percent to about 13 weight percent; ash content rangesfrom between about 2.5 weight percent to about 7.5 weight percent; watercontent ranges from between about 2 weight percent to about 10 weightpercent; total fat content ranges from between about 5 weight percent toabout 60 weight percent; palmitoleic acid content ranges from betweenabout 5 weight percent to about 60 weight percent; linoleic acid contentranges from between about 5 weight percent to about 60 weight percent;alpha-linoleic acid content ranges from between about 5 weight percentto about 60 weight percent; oleic acid content ranges from between about5 weight percent to about 60 weight percent; gamma-linoleic acid contentranges from between about 5 weight percent to about 60 weight percent;stearic acid content ranges from between about 5 weight percent to about60 weight percent; potassium content ranges from between about 25 ppm toabout 1 weight percent; chloride content ranges from between about 50ppm to about 1 weight percent; calcium content ranges from between about50 ppm to about 1 weight percent; phosphorous content ranges frombetween about 50 ppm to about 1 weight percent; magnesium content rangesfrom between about 50 ppm to about 1 weight percent; zinc content rangesfrom between about 50 ppm to about 1 weight percent; iron content rangesfrom between about 25 ppm to about 1500 ppm; sodium content ranges frombetween about 1500 ppm to about 5500 ppm; manganese content ranges frombetween about 50 ppm to about 1 weight percent; copper content rangesfrom between about 50 ppm to about 1 weight percent; iodine contentranges from between about 50 ppm to about 1 weight percent; seleniumcontent ranges from between about 50 ppm to about 1 weight percent;molybdenum content ranges from between about 50 ppm to about 1 weightpercent; Vitamin B1 content ranges from between about 15 ppm to about 15weight percent; Vitamin B2 content ranges from between about 15 ppm toabout 15 weight percent; Vitamin B12 content ranges from between about15 ppm to about 15 weight percent; Vitamin E content ranges from betweenabout 15 ppm to about 15 weight percent; Vitamin A content ranges frombetween about 15 ppm to about 15 weight percent; niacin content rangesfrom between about 50 ppm to about 5 weight percent; taurine contentranges from between about 50 ppm to about 5 weight percent; glucuronicacid content ranges from between about 50 ppm to about 5 weight percent;malic acid content ranges from between about 50 ppm to about 5 weightpercent; N-acetyl L tyrosine content ranges from between about 50 ppm toabout 5 weight percent; L-phenylalanine content ranges from betweenabout 50 ppm to about 5 weight percent; caffeine content ranges frombetween about 50 ppm to about 5 weight percent; citicoline contentranges from between about 50 ppm to about 5 weight percent; insect bulkdensity ranges from between about 3.5 pounds per cubic foot to about14.999 pounds per cubic foot; ground insect bulk density ranges frombetween about 15 pounds per cubic foot to about 50 pounds per cubicfoot.

FIG. 41A

FIG. 41A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing an insect feeding chamber having egg-laying        insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) introducing said enhanced feedstock into said insect feeding        chamber to feed the egg-laying insects present therein;    -   (d) removing a portion of said egg-laying insects from said        insect feeding chamber by applying a vacuum with a velocity        pressure range from about 0.001 inches of water to about 400        inches of water and at velocity from about 0.05 feet per second        to about 1500 feet per second. In embodiments, the insect        feeding chamber may operate at an enhanced feedstock to insect        ratio ranging from between about 1 ton of enhanced feedstock per        ton of insects produced to about 5 tons of enhanced feedstock        per ton of insects produced. In embodiments, the feeding chamber        operates at a temperature ranging from between 50 degrees        Fahrenheit to about 120 degrees Fahrenheit. In embodiments, the        feeding chamber operates at a pressure ranging from between 12        psia to about 16 psia.

FIG. 41B

FIG. 41B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing an insect feeding chamber having egg-laying        insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) introducing said enhanced feedstock into said insect feeding        chamber to feed the egg-laying insects present therein;    -   (d) removing a portion of said egg-laying insects from said        insect feeding chamber by vibrating at least a portion of said        insect feeding chamber. In embodiments, the insect feeding        chamber may operate at an enhanced feedstock to insect ratio        ranging from between about 1 ton of enhanced feedstock per ton        of insects produced to about 5 tons of enhanced feedstock per        ton of insects produced. In embodiments, the feeding chamber        operates at a temperature ranging from between 50 degrees        Fahrenheit to about 120 degrees Fahrenheit. In embodiments, the        feeding chamber operates at a pressure ranging from between 12        psia to about 16 psia.

FIG. 42A

FIG. 42A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing an insect feeding chamber having egg-laying        insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) introducing said enhanced feedstock into said insect feeding        chamber to feed the egg-laying insects present therein;    -   (d) removing at least a portion of eggs laid by the egg-laying        insects;    -   (e) incubating at least a portion of the removed eggs;    -   (f) hatching at least a portion of incubated eggs;    -   (g) introducing a portion of hatched insects into said insect        feeding chamber;    -   (h) removing a portion of said egg-laying insects said insect        feeding chamber by applying a vacuum with a velocity pressure        range from about 0.001 inches of water to about 400 inches of        water and at velocity from about 0.05 feet per second to about        1500 feet per second.

FIG. 42B

FIG. 42B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing an insect feeding chamber having egg-laying        insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) introducing said enhanced feedstock into said insect feeding        chamber to feed the egg-laying insects present therein;    -   (d) removing at least a portion of eggs laid by the egg-laying        insects;    -   (e) incubating at least a portion of the removed eggs;    -   (f) hatching at least a portion of incubated eggs;    -   (g) introducing a portion of hatched insects into said insect        feeding chamber;    -   (h) removing a portion of said egg-laying insects from said        insect feeding chamber by vibrating at least a portion of said        insect feeding chamber.

FIG. 43A

FIG. 43A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing a plurality of insect feeding chambers having        egg-laying insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) apportioning said enhanced feedstock into a plurality of        enhanced feedstock streams;    -   (d) introducing said plurality of enhanced feedstock streams        into said plurality of insect feeding chambers to feed the        egg-laying insects present therein;    -   (e) removing at least a portion of eggs laid by the egg-laying        insects;    -   (f) incubating at least a portion of the removed eggs;    -   (g) hatching at least a portion of incubated eggs;    -   (h) introducing a portion of hatched insects into at least one        of the plurality of insect feeding chambers;    -   (i) removing a portion of said egg-laying insects from said        plurality of insect feeding chambers by applying a vacuum with a        velocity pressure range from about 0.001 inches of water to        about 400 inches of water and at velocity from about 0.05 feet        per second to about 1500 feet per second.

FIG. 43B

FIG. 43B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing a plurality of insect feeding chambers having        egg-laying insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) apportioning said enhanced feedstock into a plurality of        enhanced feedstock streams;    -   (d) introducing said plurality of enhanced feedstock streams        into said plurality of insect feeding chambers to feed the        egg-laying insects present therein;    -   (e) removing at least a portion of eggs laid by the egg-laying        insects;    -   (f) incubating at least a portion of the removed eggs;    -   (g) hatching at least a portion of incubated eggs;    -   (h) introducing a portion of hatched insects into at least one        of the plurality of insect feeding chambers;    -   (i) removing a portion of said egg-laying insects from said        plurality of insect feeding chambers by vibrating at least a        portion of said plurality of insect feeding chambers.

FIG. 44A

FIG. 44A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing a plurality of insect feeding chambers having        egg-laying insects of said order present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) apportioning said enhanced feedstock into a plurality of        enhanced feedstock streams;    -   (d) introducing said plurality of enhanced feedstock streams        into said plurality of insect feeding chambers to feed the        egg-laying insects present therein; and,    -   (e) removing a portion of said egg-laying insects from said        plurality of insect feeding chambers by applying a vacuum with a        velocity pressure range from about 0.001 inches of water to        about 400 inches of water and at velocity from about 0.05 feet        per second to about 1500 feet per second. In embodiments, the        insect feeding chamber may operate at an enhanced feedstock to        insect ratio ranging from between about 1 ton of enhanced        feedstock per ton of insects produced to about 5 tons of        enhanced feedstock per ton of insects produced. In embodiments,        the feeding chamber operates at a temperature ranging from        between 50 degrees Fahrenheit to about 120 degrees Fahrenheit.        In embodiments, the feeding chamber operates at a pressure        ranging from between 12 psia to about 16 psia.

FIG. 44B

FIG. 44B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

-   -   (a) providing a plurality of insect feeding chambers having        egg-laying insects of said order present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) apportioning said enhanced feedstock into a plurality of        enhanced feedstock streams;    -   (d) introducing said plurality of enhanced feedstock streams        into said plurality of insect feeding chambers to feed the        egg-laying insects present therein; and,    -   (e) removing a portion of said egg-laying insects from said        plurality of insect feeding chambers by vibrating at least a        portion of said plurality of insect feeding chambers.

In embodiments, the insect feeding chamber may operate at an enhancedfeedstock to insect ratio ranging from between about 1 ton of enhancedfeedstock per ton of insects produced to about 5 tons of enhancedfeedstock per ton of insects produced. In embodiments, the feedingchamber operates at a temperature ranging from between 50 degreesFahrenheit to about 120 degrees Fahrenheit. In embodiments, the feedingchamber operates at a pressure ranging from between 12 psia to about 16psia.

FIG. 45A

FIG. 45A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects to generate a multifunctional flourcomposition. In embodiments, the present disclosure describes a methodfor raising Orthoptera order of insects to generate a multifunctionalflour composition, the method comprising:

-   -   (a) providing a plurality of insect feeding chambers having        egg-laying insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) apportioning said enhanced feedstock into a plurality of        enhanced feedstock streams;    -   (d) introducing said plurality of enhanced feedstock streams        into said plurality of insect feeding chambers to feed the        egg-laying insects present therein;    -   (e) removing at least a portion of eggs laid by the egg-laying        insects;    -   (f) incubating at least a portion of the removed eggs;    -   (g) hatching at least a portion of incubated eggs;    -   (h) introducing a portion of hatched insects into at least one        of the plurality of insect feeding chambers;    -   (i) removing a portion of said egg-laying insects from said        plurality of insect feeding chambers;    -   (j) grinding a portion of the removed insects to form a stream        of ground insects;    -   (k) creation of a multifunctional flour composition by mixing        ground insects of step (j) with one or more ingredients from the        group consisting of fiber-starch materials, binding agents,        density improving textural supplements, moisture improving        textural supplements, and cannabis enhancers.

FIG. 45B

FIG. 45B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional flourcomposition. In embodiments, the present disclosure describes a methodfor raising Orthoptera order of insects to generate a multifunctionalflour composition, the method comprising:

-   -   (a) providing a plurality of insect feeding chambers having        egg-laying insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) apportioning said enhanced feedstock into a plurality of        enhanced feedstock streams; introducing said plurality of        enhanced feedstock streams into said plurality of insect feeding        chambers to feed the egg-laying insects present therein;    -   (d) removing at least a portion of eggs laid by the egg-laying        insects;    -   (e) incubating at least a portion of the removed eggs;    -   (f) hatching at least a portion of incubated eggs;    -   (g) introducing a portion of hatched insects into at least one        of the plurality of insect feeding chambers;    -   (h) removing a portion of said egg-laying insects from said        plurality of insect feeding chambers;    -   (i) removing pathogens from a portion of the removed insects to        form a stream of pathogen-depleted insects;    -   (j) creation of a multifunctional flour composition by mixing a        portion of the stream of pathogen-depleted insects of step (i)        with one or more ingredients from the group consisting of        fiber-starch materials, binding agents, density improving        textural supplements, moisture improving textural supplements,        and cannabis enhancers.

FIG. 46

FIG. 46 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional flourcomposition. In embodiments, the present disclosure describes a methodfor raising Orthoptera order of insects to generate a multifunctionalflour composition, the method comprising:

-   -   (a) providing an insect feeding chamber having egg-laying        insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) introducing said enhanced feedstock into said insect feeding        chamber to feed the egg-laying insects present therein;    -   (d) removing at least a portion of eggs laid by the egg-laying        insects;    -   (e) incubating at least a portion of the removed eggs;    -   (f) hatching at least a portion of incubated eggs;    -   (g) introducing a portion of hatched insects into said insect        feeding chamber;    -   (h) removing a portion of said egg-laying insects from said        insect feeding chamber;    -   (i) grinding a portion of the removed insects to form a stream        of ground insects;    -   (j) creation of a multifunctional flour composition by mixing        ground insects of step (i) with one or more ingredients from the        group consisting of fiber-starch materials, binding agents,        density improving textural supplements, moisture improving        textural supplements, and cannabis enhancers.

FIG. 47

FIG. 47 shows one non-limiting embodiment of a method for raisingOrthoptera order of insects for the separation of lipids containedwithin said insects. In embodiments, the present disclosure describes amethod for raising Orthoptera order of insects to extract lipidscontained within said insects, the method comprising:

-   -   (a) providing an insect feeding chamber having egg-laying        insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) introducing said enhanced feedstock into said insect feeding        chamber to feed the egg-laying insects present therein;    -   (d) removing at least a portion of eggs laid by the egg-laying        insects;    -   (e) incubating at least a portion of the removed eggs;    -   (f) hatching at least a portion of incubated eggs;    -   (g) introducing a portion of hatched insects into said insect        feeding chamber;    -   (h) removing a portion of said egg-laying insects from said        insect feeding chamber;    -   (i) extracting lipids from a portion of the removed insects.

FIG. 48

FIG. 48 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects for the extraction of lipids. Inembodiments, the present disclosure describes a method for raisingOrthoptera order of insects to generate a multifunctional flourcomposition, the method comprising:

-   -   (a) providing a plurality of insect feeding chambers having        egg-laying insects present therein;    -   (b) mixing feedstock with one or more additives from the group        consisting of water, minerals, vitamins, and polymer to form an        enhanced feedstock;    -   (c) apportioning said enhanced feedstock into a plurality of        enhanced feedstock streams; introducing said plurality of        enhanced feedstock streams into said plurality of insect feeding        chambers to feed the egg-laying insects present therein;    -   (d) removing at least a portion of eggs laid by the egg-laying        insects;    -   (e) incubating at least a portion of the removed eggs;    -   (f) hatching at least a portion of incubated eggs;    -   (g) introducing a portion of hatched insects into at least one        of the plurality of insect feeding chambers;    -   (h) removing a portion of said egg-laying insects from said        plurality of insect feeding chambers;    -   (i) extracting lipids from a portion of the removed insects.

Thus, specific systems and methods of an Insect ProductionSuperstructure System (IPSS) have been disclosed. It should be apparent,however, to those skilled in the art that many more modificationsbesides those already described are possible without departing from theinventive concepts herein. The inventive subject matter, therefore, isnot to be restricted except in the spirit of the disclosure.

Thus, the applicant(s) should be understood to have support to claim andmake a statement of invention to at least: i) each of the processdevices as herein disclosed and described, ii) the related methodsdisclosed and described, iii) similar, equivalent, and even implicitvariations of each of these devices and methods, iv) those alternativedesigns which accomplish each of the functions shown as are disclosedand described, v) those alternative designs and methods which accomplisheach of the functions shown as are implicit to accomplish that which isdisclosed and described, vi) each feature, component, and step shown asseparate and independent inventions, vii) the applications enhanced bythe various systems or components disclosed, viii) the resultingproducts produced by such systems or components, ix) each system,method, and element shown or described as now applied to any specificfield or devices mentioned, x) methods and apparatuses substantially asdescribed hereinbefore and with reference to any of the accompanyingexamples, xi) the various combinations and permutations of each of theelements disclosed, xii) each potentially dependent claim or concept asa dependency on each and every one of the independent claims or conceptspresented, and xiii) all inventions described herein.

With regard to claims whether now or later presented for examination, itshould be understood that for practical reasons and so as to avoid greatexpansion of the examination burden, the applicant may at any timepresent only initial claims or perhaps only initial claims with onlyinitial dependencies. Support should be understood to exist to thedegree required under new matter laws—including but not limited toEuropean Patent Convention Article 123(2) and United States Patent Law35 USC 132 or other such laws—to permit the addition of any of thevarious dependencies or other elements presented under one independentclaim or concept as dependencies or elements under any other independentclaim or concept. In drafting any claims at any time whether in thisapplication or in any subsequent application, it should also beunderstood that the applicant has intended to capture as full and broada scope of coverage as legally available. To the extent thatinsubstantial substitutes are made, to the extent that the applicant didnot in fact draft any claim so as to literally encompass any particularembodiment, and to the extent otherwise applicable, the applicant shouldnot be understood to have in any way intended to or actuallyrelinquished such coverage as the applicant simply may not have beenable to anticipate all eventualities; one skilled in the art, should notbe reasonably expected to have drafted a claim that would have literallyencompassed such alternative embodiments.

Further, if or when used, the use of the transitional phrase“comprising” is used to maintain the “open-end” claims herein, accordingto traditional claim interpretation. Thus, unless the context requiresotherwise, it should be understood that the term “comprise” orvariations such as “comprises” or “comprising”, are intended to implythe inclusion of a stated element or step or group of elements or stepsbut not the exclusion of any other element or step or group of elementsor steps. Such terms should be interpreted in their most expansive formso as to afford the applicant the broadest coverage legally permissible.

Finally, any claims set forth at any time are hereby incorporated byreference as part of this description of the inventive technology, andthe applicant expressly reserves the right to use all of or a portion ofsuch incorporated content of such claims as additional description tosupport any of or all of the claims or any element or component thereof,and the applicant further expressly reserves the right to move anyportion of or all of the incorporated content of such claims or anyelement or component thereof from the description into the claims orvice-versa as necessary to define the matter for which protection issought by this application or by any subsequent continuation, division,or continuation-in-part application thereof, or to obtain any benefitof, reduction in fees pursuant to, or to comply with the patent laws,rules, or regulations of any country or treaty, and such contentincorporated by reference shall survive during the entire pendency ofthis application including any subsequent continuation, division, orcontinuation-in-part application thereof or any reissue or extensionthereon.

Although the foregoing text sets forth a detailed description ofnumerous different embodiments of the disclosure, it should beunderstood that the scope of the disclosure is defined by the words ofthe claims set forth at the end of this patent. The detailed descriptionis to be construed as exemplary only and does not describe everypossible embodiment of the disclosure because describing every possibleembodiment would be impractical, if not impossible. Numerous alternativeembodiments could be implemented, using either current technology ortechnology developed after the filing date of this patent, which wouldstill fall within the scope of the claims defining the disclosure.

Thus, many modifications and variations may be made in the techniquesand structures described and illustrated herein without departing fromthe spirit and scope of the present disclosure. Accordingly, it shouldbe understood that the methods and apparatus described herein areillustrative only and are not limiting upon the scope of the disclosure.

Unless the context dictates the contrary, all ranges set forth hereinshould be interpreted as being inclusive of their endpoints, andopen-ended ranges should be interpreted to include commerciallypractical values. Similarly, all lists of values should be considered asinclusive of intermediate values unless the context indicates thecontrary.

The recitation of ranges of values herein is merely intended to serve asa shorthand method of referring individually to each separate valuefalling within the range. Unless otherwise indicated herein, eachindividual value is incorporated into the specification as if it wereindividually recited herein. All methods described herein can beperformed in any suitable order unless otherwise indicated herein orotherwise clearly contradicted by context. The use of any and allexamples, or exemplary language (e.g., “such as”) provided with respectto certain embodiments herein is intended merely to better illuminatethe disclosure and does not pose a limitation on the scope of thedisclosure otherwise claimed. No language in the specification should beconstrued as indicating any non-claimed element essential to thepractice of the disclosure.

Groupings of alternative elements or embodiments of the disclosuredisclosed herein are not to be construed as limitations. Each groupmember can be referred to and claimed individually or in any combinationwith other members of the group or other elements found herein. One ormore members of a group can be included in, or deleted from, a group forreasons of convenience and/or patentability. When any such inclusion ordeletion occurs, the specification is herein deemed to contain the groupas modified thus fulfilling the written description of all Markushgroups used in the appended claims.

It should be apparent to those skilled in the art that many moremodifications besides those already described are possible withoutdeparting from the inventive concepts herein. The inventive subjectmatter, therefore, is not to be restricted except in the spirit of theappended claims. Moreover, in interpreting both the specification andthe claims, all terms should be interpreted in the broadest possiblemanner consistent with the context. In particular, the terms “comprises”and “comprising” should be interpreted as referring to elements,components, or steps in a non-exclusive manner, indicating that thereferenced elements, components, or steps may be present, or utilized,or combined with other elements, components, or steps that are notexpressly referenced. Where the specification claims refer to at leastone of something selected from the group consisting of A, B, C . . . andN, the text should be interpreted as requiring only one element from thegroup, not A plus N, or B plus N, etc.

Unless defined otherwise, all technical and scientific terms used hereinhave the same meaning as commonly understood by one of ordinary skill inthe art to which this invention belongs. Although any methods andmaterials similar or equivalent to those described herein can also beused in the practice or testing of the present invention, a limitednumber of the exemplary methods and materials are described herein.

It must be noted that as used herein and in the appended claims, thesingular forms “a”, “an”, and “the” include plural referents unless thecontext clearly dictates otherwise.

The invention claimed is:
 1. An Insect Production Superstructure System(IPSS), the IPSS includes: (a) an insect feeding chamber having aninterior and having insects present therein; (b) a temperature sensorconfigured to measure the temperature within the interior of the insectfeeding chamber; (c) an air supply fan equipped with an air supply fanmotor, the air supply fan provides an air supply to an air heater; (d)the air heater is configured to accept the air supply from the airsupply fan and produce a heated air supply to heat the interior of theinsect feeding chamber, wherein the air supply is heated by the airheater which is operatively connected to an energy source selected fromthe group consisting of electricity, natural gas, combustion, solar, andsteam; (e) a filter configured to accept a particulate and gas mixturefrom the interior of the insect feeding chamber, the filter separatesparticulates from the particulate and gas mixture and outputs aparticulate-depleted gas stream, the particulate-depleted gas stream hasa reduced amount of particulates relative to the particulate and gasmixture; (f) an evacuation fan configured to evacuate at least a portionof the particulate-depleted gas stream from the filter, the evacuationfan is equipped with a motor; and (g) a refrigerant configured to betransferred from a compressor to a condenser, from the condenser to anevaporator, and from the evaporator to the compressor, the compressor isin fluid communication with the condenser, the condenser is in fluidcommunication with the evaporator, the evaporator is in fluidcommunication with the compressor, the evaporator is configured toevaporate the refrigerant to absorb heat from the interior of the insectfeeding chamber.
 2. The IPSS according to claim 1, further comprising:(h) a network of cells positioned within the interior of the insectfeeding chamber for insects to live in, the network of cells have afirst set of openings positioned at a first end and have a second set ofopenings positioned at a second end, insects live in passageways betweenthe first set of openings and the second set of openings.
 3. The IPSSaccording to claim 1, further comprising: a computer; the temperaturesensor is configured to measure the temperature of the interior of saidinsect feeding chamber and send a signal to the computer; and the airsupply fan motor is equipped with a controller, the controller is inoperative connection with said configured to input and/or output asignal computer; wherein: the computer automatically adjusts thetemperature within the interior of the insect feeding chamber to atemperature ranging from between 60 degrees Fahrenheit to 100 degreesFahrenheit by operating the air supply fan motor in response to theinput signal from the temperature sensor.
 4. The IPSS according to claim1, further comprising: a computer; and the temperature sensor isconfigured to measure the temperature within the interior of the insectfeeding chamber and send a signal to the computer; wherein: the computerautomatically adjusts the temperature within the interior of the insectfeeding chamber to a temperature ranging from between 60 degreesFahrenheit to 100 degrees Fahrenheit by adjusting the temperature of theair heater in response to the input signal from the temperature sensor.5. The IPSS according to claim 1, further comprising: a computer; andthe air supply fan motor is equipped with a controller, the controlleris in operative connection with said computer; wherein: the air heaterand/or the air supply fan motor and/or the controller arecommunicatively coupled to the computer, the computer comprises aprocessor and a memory, the memory includes code configured to cause theprocessor to transmit a signal to the air heater and/or the air supplyfan motor and/or the controller to control the temperature within theinterior of the insect feeding chamber to a temperature ranging frombetween 60 degrees Fahrenheit to 100 degrees Fahrenheit.
 6. The IPSSaccording to claim 1, wherein: the filter includes an entry section andan exit section, a filter element is positioned in between the entrysection from the exit section, the filter element permits theparticulate-depleted gas stream to flow through the filter element fromthe entry section and into the exit section.
 7. The IPSS according toclaim 1, further comprising: (h) a mixing tank having an interior, themixing tank has an input configured to accept at least a portion of theinsects from the interior of the insect feeding chamber, the mixing tankmixes water with the insects to form a liquid mixture, the mixing tankhas an output configured to transfer the liquid mixture to a supplypump; (i) the supply pump is configured to transfer the liquid mixturefrom the interior of the mixing tank to a filter; (j) the filter isconfigured to filter the liquid mixture supplied by the supply pump toform an exoskeleton-depleted insect liquid mixture that has a reducedamount of exoskeleton relative to the liquid mixture supplied by thesupply pump; (k) an evaporator configured to accept theexoskeleton-depleted insect liquid mixture from the filter, theevaporator is configured to evaporate at least a portion of the liquidfrom the exoskeleton-depleted insect liquid mixture to form vaporizedliquid and liquid-depleted insects, the liquid-depleted insects have areduced amount of liquid relative to the exoskeleton-depleted insectliquid mixture; (l) a condenser configured to accept and condense thevaporized liquid from the evaporator, gas is evacuated from thecondenser and is transferred to a vacuum system; and (m) the vacuumsystem is configured to accept the gas from the condenser, at least aportion of the gas is discharged from the vacuum system via a gastransfer line.
 8. The IPSS according to claim 1, further comprising: (h)a water bath configured to accept at least a portion of the insects fromthe interior of the insect feeding chamber; and (i) a grinder configuredto grind at least a portion of the insects that are discharged from thewater bath to form ground insects.
 9. The IPSS according to claim 1,further comprising: (h) a mixing tank configured to accept at least aportion of the insects from the interior of the insect feeding chamber,the insects are mixed with water within the mixing tank to form amultifunctional flour and water mixture; (i) a shaping system configuredto shape at least a portion of the multifunctional flour and watermixture to form a shaped multifunctional flour mixture; (j) a cookingsystem configured to cook at least a portion of the shapedmultifunctional flour mixture to form a cooked multifunctional flourmixture; and (k) a flavoring system configured to flavor the cookedmultifunctional flour mixture provided from the cooking system to form aflavored multifunctional flour mixture.
 10. The IPSS according to claim9, wherein: the shaping system includes an extrusion system, theextrusion system forms the shaped multifunctional flour mixture bypressing the multifunctional flour and water mixture through a die, thedie has a fixed cross-sectional profile and is configured to accept themultifunctional flour and water mixture and press it into an extrudate.11. The IPSS according to claim 9, wherein: the cooking system includesone or more cooking systems selected from the group consisting of adryer, a pressure cooker, a dehydrator, and a freeze dryer, the cookingsystem is configured cook the shaped multifunctional flour mixture toform a cooked multifunctional flour mixture.
 12. The IPSS according toclaim 9, wherein: the cooking system includes one or more cookingsystems selected from the group consisting an oven and a fryer, thecooking module is configured cook the shaped multifunctional flourmixture to form a cooked multifunctional flour mixture.
 13. The IPSSaccording to claim 9, wherein: the flavoring system is configured toprovide contact between flavoring and the cooked multifunctional flourmixture to form a flavored multifunctional flour mixture.
 14. The IPSSaccording to claim 13, wherein: the flavoring system includes a tumbler,the tumbler has a motor, the tumbler rotates and is configured toprovide contact between the flavoring and the cooked multifunctionalflour mixture to form a flavored multifunctional flour mixture, thetumbler rotates at a revolution per minute (RPM) ranging from between 3RPM to 20 RPM.
 15. The IPSS according to claim 1, further comprising:(h) a feedstock distributor positioned within the interior of the insectfeeding chamber, the feedstock distributor is configured to accept asource of feedstock from a conveyor and make the feedstock; and (i) theconveyor is configured to introduce the feedstock to the feedstockdistributor; wherein: the feedstock is comprised of one or morematerials selected from the group consisting of agriculture residue,alcohol production coproducts, animal waste, bio-waste, compost, cropresidues, energy crops, fermentation waste, fermentative process wastes,food processing residues, food waste, garbage, industrial waste,livestock waste, municipal solid waste, plant matter, poultry wastes,rice straw, sewage, spent grain, spent microorganisms, urban waste,vegetative material, and wood waste.
 16. The IPSS according to claim 1,further comprising: (h) a first water treatment unit configured toaccept a source of water and remove contaminants therefrom, the firstwater treatment unit includes one or more water treatment units selectedfrom the group consisting of an adsorbent, ion-exchange resin, catalyst,and activated carbon; (i) a valve configured to accept at least aportion of the water from the first water treatment unit; and (j) adistributor positioned within the interior of the insect feedingchamber, the distributor is configured to accept at least a portion ofthe water discharged from the valve and make the water available to theinsects.
 17. The IPSS according to claim 1, further comprising: (h) afirst water treatment unit configured to accept a source of water andremove contaminants therefrom, the first water treatment unit includesone or more water treatment units selected from the group consisting ofan adsorbent, ion-exchange resin, catalyst, and activated carbon; (i) awater supply pump configured to accept at least a portion of the waterfrom the first water treatment unit; (j) a valve configured to accept atleast a portion of the water from the water supply pump; and (k) adistributor positioned within the interior of the insect feedingchamber, the distributor is configured to accept at least a portion ofthe water discharged from the valve and make the water available to theinsects.
 18. An Insect Production Superstructure System (IPSS), the IPSSincludes: (a) an insect feeding chamber having an interior and havinginsects present therein; (b) a computer; (c) a temperature sensorconfigured to measure the temperature within the interior of the insectfeeding chamber and send a signal to the computer; (d) an air supply fanequipped with an air supply fan motor, the air supply fan provides anair supply to an air heater; (e) the air heater is configured to acceptthe air supply from the air supply fan and produce a heated air supplyto heat the interior of the insect feeding chamber; (f) a filterconfigured to accept a particulate and gas mixture from the interior ofthe insect feeding chamber, the filter separates particulates from theparticulate and gas mixture and outputs a particulate-depleted gasstream, the particulate-depleted gas stream) has a reduced amount ofparticulates relative to the particulate and gas mixture; (g) anevacuation fan that is configured to evacuate at least a portion of theparticulate-depleted gas stream from the filter, the evacuation fan isequipped with a motor; and (h) a refrigerant configured to betransferred from a compressor to a condenser, from the condenser to anevaporator, and from the evaporator to the compressor, the compressor isin fluid communication with the condenser, the condenser is in fluidcommunication with the evaporator, the evaporator is in fluidcommunication with the compressor, the evaporator is configured toevaporate the refrigerant to absorb heat from the interior of the insectfeeding chamber.
 19. The IPSS according to claim 18, further comprising:(i) a mixing tank having an interior, the mixing tank has an inputconfigured to accept at least a portion of the insects from the interiorof the insect feeding chamber, the mixing tank mixes water with theinsects to form a liquid mixture, the mixing tank has an outputconfigured to transfer the liquid mixture to a supply pump; (j) thesupply pump is configured to transfer the liquid mixture from theinterior of the mixing tank to a filter; (k) the filter is configured tofilter the liquid mixture supplied by the supply pump to form anexoskeleton-depleted insect liquid mixture that has a reduced amount ofexoskeleton relative to the liquid mixture supplied by the supply pump;(l) an evaporator configured to accept the exoskeleton-depleted insectliquid mixture from the filter, the evaporator is configured toevaporate at least a portion of the liquid from the exoskeleton-depletedinsect liquid mixture to form vaporized liquid and liquid-depletedinsects, the liquid-depleted insects have a reduced amount of liquidrelative to the exoskeleton-depleted insect liquid mixture; and (m) acondenser configured to accept and condense the vaporized liquid fromthe evaporator.
 20. A system to produce liquid-depleted insects, thesystem includes: (a) a water treatment unit configured to accept asource of water and produce treated water therefrom, the water treatmentunit includes one or more water treatment units selected from the groupconsisting of an adsorbent, an ion-exchange resin, a catalyst, andactivated carbon; (b) a mixing tank having an interior, the mixing tankis configured to accept insects and at least a portion of the treatedwater from the water treatment unit, the mixing tank mixes the treatedwater with the insects to form a mixture of insects and treated water,the mixing tank is configured to transfer the mixture of insects andtreated water to a pump; (c) an evaporator configured to accept themixture of insects and treated water from the pump, the evaporator isconfigured to evaporate at least a portion of the treated water from themixture of insects and treated water to produce steam andliquid-depleted insects, the liquid-depleted insects have a reducedamount of treated water relative to the mixture of insects and treatedwater; (d) a condenser configured to accept and condense the steam fromthe evaporator, gas is evacuated from the condenser and is transferredto a vacuum system; and (e) the vacuum system is configured to acceptthe gas from the condenser, at least a portion of the gas is dischargedfrom the vacuum system via a gas transfer line.